• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A wet phosphoric acid production process comprising the attack on phosphate rock by sulfuric acid and phosphoric acid utilizing a vacuum cooling and a recirculation of the reaction slurry. The flow rates of the materials within the system are maintained at a level, relative to the rate of withdrawal of the slurry from the system, of between 300% and 4000% for the cyclic flow, between 2000% and 4000% for the vacuum cooling flow and between 500% and 2200% for the local agitation flow. Control of the flow rates according to factors including the rock analysis allows maximization of the yield of H3PO4.
    公开号:SU1068024A3
    申请号:SU782634048
    申请日:1978-07-13
    公开日:1984-01-15
    发明作者:Лоран Давистер Арман
    申请人:Сосьете Де Прэйон (Фирма)；
    IPC主号:
    专利说明:

    ABOUT
    about: oo o y
    four
    The invention relates to: a method; obtaining phosphorus; oh soric acid; o-acid pa3j; o eHi-QM a) osfatkg r-aaar of various types and can be used in the production of noj; y4e neither various forcing and sulfurous mineral fertilizers.
    There is a known method of phosphoric acid production, including the processing of crushed phosphate raw materials of phosphoric and sulfuric acid in the decomposition zones when recirculating the reaction suspension through decomposition in the amount of lCOO-1500% by weight of the suspension fed to the filtration, BaKyyM-oxjbtUKfleHMTy -pensions, crystallization of catalysts sulphate; nc, npONWBKy with its water to wash out water; processing of the raw materials into a “turn; op} -: ki slots L1 J ..
    However, with this method, ke: / “: tyvast: IK.-: lererabatmye south of raw materials.
    Isaesthen is also a half-way
    phosphoric KHCJlOTb, SKJJKl alOIlHH Obr L
    bosk and emulsified phos; Fat 1 from-about ;;,: About Kk CJ; o - ;; oK ,, diluted: PivrbJUHt .iiXri with water and in the zone once a recyr; u /; tion to susigeg.ich between the preheater and zonop p, -: ij: o xceHLiH iakuya-ohlgadddenie su sp; -i-a v. chrisallium acy; sulphate; a transaction of the city of the ukta from sediment, calcium; phyla; walkie-talkie, ego I; and, the removal of the water from the waters of the sulfuric acid stream, POLUS: a 3: phosphoric acid (95-96) h i 2 ,,
    However, j / OT cr; especially ats is not enough product.
    The most slimy to the technical c ;, schisti moku result; :; Lakes: Phosphoric Acid., Zcl.HygYyuIaI processing of finely graded phosphate raw materials with recycled sulfuric acid; in the zone of decomposition at pcc; gr susanzik; 5kuu: -; - ohl) kdeni-e suspension; Kpiic al / b.zasch: 1yu sulfate. about td alen-ie product from sulphate sulphate. zgal
    ipyi fml: -: walkie-talkie. ert .; .ibjbxy with rTpoivbJBMHv zozkiat, code for scrapping the CID.-I U; (as reusable phosphorus - - :: wasteklp1-and suspension | cheniah: h 30b razlochchchik ii chilled.cemie; ; remaining for filtering; Exxi .i pr.g.yukta oostsvliet 9b-96% Gz,; edemastvamkamk known ATP; soba ;; j: fiio -: - f; 3- ыш Extensive energy expenditure h .: grinding a,:;; - - not, dasta-J-OMHO Byso: Product output, as well as the inability to effect various types of raw materials, which is due to the lack of: • multiplicity of circulations.
    The purpose of the kzobretenl ;; h.;: Is; reduction of energy consumption: and from the smaller ones - up to raw materials,
     —cor3iaoiic CHO: ot; y receiving rosworn. .;::.: lot; . vk7: yuchu1ts.;, 1y g. u.uaooo-gku.; -: focFaJ.no Lo Zori 3 3C) i-MX Raa.uj.a-g a6) pcv7fioK in; sphere of sulfuric sulfur, with slots at ije rchul 4i ;; - 3.i reaction-flow control: -; and C :, one; y m-OXJ-: aldekyu suo exams, k ::; -; eTajij;: - s3 a; j,; - i 10 with lfata. ylyatsi.le,.; y; -ai; s susg; e -; zia. otd;; lnnye sediment body: g; Calczi ,, ipcivbipKy su-o -: iRow. e; : - к; .- З.жлаа аа -.ларабозкку; рь5 н кг.куУ-1: е все9 -: --- оУ -ос-фЛ-Кл: -, хи; к1лг ,, ере : zon razloenm ::. Edit 300 OJ J peaKpiik: ;; -; HO -i i.ycjr-ef-i-; : ii by weight
    . slankik, | .ost-; T1a; g elna, filter -a-fy z; .y Cg.Au.; oo: .- dg: s-,: years: e: -: zi, 1 from .lesu cycrif-- zup, postu.d-yuCHOi bch;;) - ;. ; p ;, chi: 0; a: ;; a;:; dy zone
    --Y C; ir:;: i3K ;. ABOUT . ..L With Cl; ..; Su 3 С I) 3 И Н, ПГГГУj :: a: ;;; ie. . | 3.; 1: -1.; Ation,
     .. :: esa e-L reduce rzsc: .о ;: 3.; iep: 5H.: az izdelyuenie ryr aa:., 3 .aa., uabsGP; : atz. The gulf rpmdggyo O. ,,,: d,., I .: times .. gkiov. ::: lsan; .-- ss and f; , wasp. and, aru.
    - 3. {ij .; 3 About K kz and n. zn and 1 j ku-i. Lf and o n
    Through-reaction: zones.
    Through the cooling zone
    in the reaction zone
    In tab. Table 2 presents data on the effect of the recirculation value on the thickness of the filter cake of volcanic origin (apatite). From the data given in Table 2, it follows that at recirculation values below or above the suggested 65
    ki of phosphogypsum and the residual content in it of phosphorus pentoxide a,
    Table 2 the filtration rate of phosphogypsum decreases. Therefore, the thickness of the filter cake is reduced, while
    residual content; :(;) th; -.- ::: cj.: x: j ..: you increase the size of her--,: luxmv, that is suggested; ct :: hall; -.; ::: -: - mapny.
    Example i. iuay is broken:; eni volume 3SO m io, tsag; t 32,; t / h of marcakk phosphate (33% turnover of fossil kii slot k., 4 t / h of saric acid, sre and reactive su (90), 3 hg of: h: ti K0 -,; j -: fi; o ; cam12 is free; -; c:; pHijii ,,:, 1СЛ (,; Зи; SOSTaELYaYT 4 -. 1;. ЭУ rWiJC; ;;
    phosphate - 60--7; Oh, 15 H-Jo; -. to VAPITALITY; v; fi: i fiJiO-: c ;; i: - - i3nri-.3; 1080 m3 / h IipaTrOCiCV, PS; and: pKURYATS:, and
    lead through the zone rezloke :: sp and zon- /
    OHLSLEDEELIP SOS h ;;, .ir: (P.-.
    13150 m3 / - 1 m-gi;, ;; - vonno.CH; as; G; successionstolzgol.ol: szek; p :. ; -; - h; ::
    LIZATSIG PHOSPHOGYPSE E:; - Gula:.; V CViX: l
    zi d kalm-ch: ests :: EO s - / i noccyi; df: on BpaiJiascEUMfiCu n.nocLi: i, i - g -; - ::; j; -i Bakuu 1 fkltr, Fosfog ./: ps by / z.yar; ,:, they are trekkratyoy: if; vr; vr -; pat; -; r | -o; .., :: those, and Sol :; ns: Wo; i ;;,: -; -, regulate in 3as4CKv: ocrH from Xc-tg stza phosphate and tol: l :, -KervawKy} iC get acid, SODE., jQv u.o Tolshkks rer-; eu: K (he, ,:, a ;.
    权利要求:
    Claims (1)
    [1]
    METHOD FOR PRODUCING PHOSPHORIC ACID, including treatment of crushed phosphate feedstock with reverse phosphoric and sulfuric acids in the zones' decomposition during recycling of the reaction suspension, vacuum cooling of the suspension, crystallization of calcium sulfate, filtration of the suspension, separation of the precipitate of calcium sulfate, washing it with water and returning raw water and acid for processing raw materials as a reverse phosphoric acid slots, characterized in that, in order to reduce energy consumption for grinding raw materials in the processing of various types of raw materials, h 300-4000% of the reaction slurry from the mass of the slurry entering the filtration is recirculated through the decomposition zone; 2000-4000% of the recirculated slurry from the mass of the slurry entering the filtration is recycled to the vacuum cooling zone, and 500 to 2200% are recirculated in each decomposition zone suspension from the mass of suspension entering the filtration.
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    SU420556A1|1974-03-25|
    同族专利:
    公开号 | 公开日
    OA05992A|1981-06-30|
    FR2407891B1|1982-11-05|
    NL7806776A|1979-05-08|
    US4298583A|1981-11-03|
    IN149585B|1982-01-30|
    BR7804003A|1979-05-29|
    IL54974D0|1978-08-31|
    IT7824753D0|1978-06-20|
    GB2007200B|1982-06-16|
    JO1086B1|1982-07-10|
    GB2007200A|1979-05-16|
    NZ188819A|1980-09-12|
    IT1096581B|1985-08-26|
    LU78457A1|1979-06-13|
    ZA783583B|1979-06-27|
    ES471072A1|1979-01-01|
    AU3727678A|1980-01-03|
    DE2827114A1|1979-05-10|
    CA1106137A|1981-08-04|
    BE868072A|1978-10-02|
    FR2407891A1|1979-06-01|
    IL54974A|1981-02-27|
    JPS5523082A|1980-02-19|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    BE502036A|1950-03-03|
    BE538799A|1955-06-07|1955-06-30|Union Chimique Belge Sa|
    NL274891A|1961-02-17|
    FR1323087A|1961-03-30|1963-04-05|Vacuum cooling process for multi-phase chemical treatments|
    US3257168A|1961-03-30|1966-06-21|Singmaster & Breyer|Process for manufacture of phosphoric acid|
    US3472619A|1964-03-06|1969-10-14|Singmaster & Breyer|Production of phosphoric acid and calcium sulfate|
    US3416889A|1964-06-22|1968-12-17|Whiting Corp|Process and apparatus for manufacturing phosphoric acid|
    US3522003A|1966-01-03|1970-07-28|Pullman Inc|Process and apparatus for producing phosphoric acid from phosphate rock|
    US4140748A|1976-07-07|1979-02-20|Occidental Petroleum Corporation|Hemihydrate type phosphoric acid process with crystal modifier|
    DE146443C|1976-07-07|Occidental Petroleum Corp|DE3583209D1|1984-11-05|1991-07-18|Prayon Dev Sa|CONTINUOUS PROCESS FOR PRODUCING PHOSPHORIC ACID AND CALCIUM SULFATE.|
    US5300434A|1987-11-06|1994-04-05|Washington Research Foundation|Hybridoma cell line producing an antibody to type-I collagen amino-terminal telopeptide|
    WO2010135141A1|2009-05-18|2010-11-25|Monsanto Technology Llc|Recovery of phosphorus values and salt impurities from aqueous waste streams|
    CN103303889A|2013-07-03|2013-09-18|瓮福（集团）有限责任公司|Online cleaning method for tubular reactors|
    CN103303890A|2013-07-04|2013-09-18|瓮福（集团）有限责任公司|Online reflux rinsing method for tubular reactor|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    LU78457A|LU78457A1|1977-11-04|1977-11-04|PHOSPHORIC ACID MANUFACTURING PROCESS|
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