• 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:
    For the preparation of acetic acid and acetic anhydride, methanol and methyl acetate are reacted under anhydrous conditions with carbon monoxide in the presence of a carbonyl complex of group VIII noble metals, methyl iodide, and catalyst systems containing alkali metal or quaternary organophosphonium or organoammonium acetate or iodide. The hot carbonylation mixture is depressurised, the evaporated components are added to a first distillation zone, and the remaining catalyst solution is fed back to the reaction zone. In the first distillation zone, the volatile carbonylation products are fractionally distilled; the low-boiling components methyl iodide and methyl acetate pass back into the reaction zone, and a mixture of acetic acid and acetic anhydride is obtained as a bottom product which is separated into the pure components in a second and third distillation zone.
    公开号:SU1766249A3
    申请号:SU894614443
    申请日:1989-07-12
    公开日:1992-09-30
    发明作者:Эрпенбах Хайнц；Германн Клаус；Егерс Эрхард；Коль Георг
    申请人:Хехст АГ；
    IPC主号:
    专利说明:

    Acetic students ; / hch; g; olhui lh in organic nssh-jyulenny synthesis. The goal - the prevention of corrosion, synthesis of Zed. / t reaction; th me anol i.; ei.: cetzga (; - OOn ratio from 4,6: 1, -. I dj and CO or its mixture with hydrogen in the presence of a catalyst - carbo-i-th complex under , methylsdide and .TLiSaiopa (lithium iodide acetate N-etzno / s and meth: .1l;.; etztg1). octag5o; dy-Oi it about g ostlt :: cf.1 ..: l.:.; - x .. ovec ;.
    . idazols) ng; and 6C-22C C. pressures of 30-70 bar in an anhydrous medium. Then, the mixture passing from the reaction zone passes through an additional seac- tor (to dissolve dissolved CO) at 160–220 ° V and a residence time of 2–3 min with decreasing pressure to 1-3 5 bao in the zone once the liquid, however, the main suit of volatile components is saved, and therefore, to reduce entrainment, the font of the liquid through the mist extractor feeds the first distillation zone (to separate low-boiling components). The liquid stream formed in the vapor-liquid separation zone and the fog separator is subjected to the next zone divided Jun at 95k. /. v х: .--, e;: bob x: -re one write records 01 "Often, by the way, he has developed a bit of rasorosis .. h, 1 zko / p shch1-, x pro; ov- –hlohs xe costz and is 9–20 instant instead of megalith gtz it is better to use dimethyl and office, a co and (–2 m o: -chet containing up to 5 s-0 00 fj ;, filtering glass is used in the separator: - .. fiberglass cloth 3 feeds from the reaction ZONE flow support the molar co between the maternity hospital activator, methyl iodide cm:; methlaetatatom. equal to: 18-251 78-230 :: 150-560. , the concentration of hydrogen is 0.008–0.03 mol / l. Separated; ; the volatile components from the solution katal / zzto |) by distillation in a second section ;; you will relate; 1: .--. / „About the possible method received; - ..: sing: and uksuoksto a; ngidr ldg. acid and acetic acid :; r .-.:. Ј. are highly significant; - ;; /; chesky prismguechnye purge giving them:. Wikilzcedt, G.-T.VI cellulose acetate preparations.
    Known to sooooo cosme or acetic acid. Yes. According to this cno-jj y
    OR DI METLIL TH Zfir YOD / 1-1
    circumventing the metalworking action of the presence of catal zatsoi, s: with the noble metal V rpy; v chesky S11 system, s.-than synthon: s,.:.
    iiKTi / SBSTOGS V CCdiCTwBc TOpa / lc
    not
    poluneni crxeoi y;.:; many anhydride, poi
    INITIAL CMSCi-i SOS G
    alcohol, however, is not stoichiometric: about ether.
    Such rekakinin.e demolish ho.,,. A number with acetic acid and the reaction ;; -; o. TOTAL SUBSTITUTIONAL-EHD: CO-i,: J, i -; - ::,.,.,...
    also contain the back, - high-corrosion ps otkos,.; x. most technically. i--: "Her1- - also go attitude; s-tats lg.1 -: STU, - ..
    HASGELLAI, AND POSTLY; Yiwu PRIMOD T ;; - ;;:,:
     to the road..v: l-, lth o;,.-.-. ; g ..-, measures to tantalum.
    The purpose of isoretch: -; : -: -: e; - .g ....:; - ..: ..:. corrosion,
    THIS IS ACHIEVED WITH P O S O-b ..-.-: .-: i.,;
    to the invention, which is: o-that methanol and EHZAGEN methyl acetate -;.; h: mode e in molar ratio:.;. ; 4.64: 1 to 1: 8. anhydrous conditions at Tsiv rnepdTy-H-: l - up to 220 ° C and pressures from 30 ds Y0; h as an activator kagalit /; Th -;, :: o; ;.:; n
    WE USE SCHSPYT / II /; THIS: methyl methylbromyl iodide iodide and Fr. :; .-. -dimethylimidazolyl. . Well, the reaction mixture is passed to the CPCR ;, nl l, and p about a and a and c e: s; p b a i; ; and.-,.-. dissolved mons:
    Catal And plzka contains and szzdn prefer to use
    What is the additional qualification of the Chhtmvatsrz uni-N 0 Kzing g: -.ztdz-o / nor for the bonds. ; h -: h; about
    zirconium, vanadium,. reni or it is possible l p: /: -;: - r and also i -J- з: з ззззз ПНИКЕЛЯ, SRI D,: - | .3. F-MeTZL-Z-GNHSZZIZIZYIODPZ N1zrem preyyzyyki from / pzz-z.x Zeyzste5. and g -, 4 - l v and h. .- g; and and and: ;: and h .: in the reaction zone of the enterprise; 3. ch- / g gi; lml. N.7zz, zid, ..- gh. - natural flows returned to zonul-l-llozid s others. Konzsnt aiin; noz1v; 1 reaction kztzl zztorz solution; and leghokie-ru.ch.).:. and h; lz c the reaction mixture can melt methyl iodide. 1.ac & ha but ; ah- G8 of the used substances of methanol and 10 methyl acetate, is from 9 to 20 minutes;
     t jyQ CHYY; - iT1 / 1L - .., - ;, TSG 33: -; L: CT
    KZ dimethyl s ..: o1kas5s: -: silt; ...- complexes; e5lacsro.:; chye
     rc.aabSJNio-vi: -;.:; :.; .. I lc-hvi. j sohy.:, v ;. Apt::.;.; Z; /. C. Re and, b; Ni, hr, dem. HRSS TBIN.:,.:: .S with; -; with rf. ,,;,. 4 zyut1 b with;: b:, D) 1ET- :. s: gzk. :: and;:; lasgssl) gzno i hl / from /:,;; j m OS cot / r: about jj TJ n i--. about; -c / j: h::: i. - -fi-ss .... so.:;, - ;: rszg- (e, r-imer
    ... i "from 0.008 to 03, .yy ,, /; /, ::;. .; -. . .,: .- г- 0.0; TO S.L. vr,: /. : -: o
    neither ro.;. galeleg and p oo: -.- ;, and h з.;: - s / tst3 -r /; mo -, -: з: -ю ::, з: -; л, .з t ТЗ: ито у
    MONRSKSIDZ and aezzodiags- with G.O. - A - 3 - Ssmes igonsonsoxidis 3 ozd; / i: ods-2e, otak, .- lu
    OO / JiJ OSDZHMT TO 5 GC-. V; CHSD1 303 :: j i ;; i-; iS ZZZ.ZTZV
    G: -; 3-NHS DZL / H. e T i .- .-- T O:.: .- Vf; o-3 v C H C: ..- 3: ;;. . ..
    oij / ibHVX.i TCdHb yi3 3 ЗКЗ. :., .LOX, h t-3 t; ;. :: ZP; Gi / lC; | OL o &D.; 3:, Ss Ch. ivr: 33; 3: 3 T333JL3; -.
    /: Lerod i-; e oo zatozno dolhen h / n: -30 Gz
    : eLiiu; - ,; zonigi ;; oea; iu. paoni-ic.i. - g
    sol., me mo oschsiah /; eoods; s RS-GAYUI.-.
    On the other hand, a and: About constant: - L:; and .3S-zr 3: - 3; 3; -z c.ve-zg. .zizyoztaz; -: about zodorode up to 5 oy.% put-yus yzzgz -oz.zz | 3 -5 &;; - zy lgssob.
    skgzych STZ on the activity of the G-th accident: -: h g ieszgz y, - til cetat; MA) -.
    torus, H-.J lechizhovt select zzozgg with: oszbame: tnlzl (СНзС -; гз, then f or for the year 24. -:; og
    FOR OZZR TZOZA: - :: i .: PRODUKTiZ DRROZZ-PROM YUZTYA. : 5 ZG ZZSZ. DEPT: tp1-, for example, 31 lddy-; designztztz .13, ,, zz: gztz z -z xsz chzzz-isz
    tylengko ko / -diya s-t and .tsiok. l l zg ;; o-; from w: - h. -. -, yi eatz.
    B quality 1; zdzzzzni drove-ze city zg.-; 3: Lsz; s 3; og. .-.
    All compounds which are hpc reactions can be used. -0; zez ™ .g ./-; ozod od 3 moksokzd
     aorims to provide; x reaction: m form a to-chtler zz s -; 8rez (-. BZODI;: the complex complex of Larronila smagorod oy4Ј in zzrz-l, ..; ..: -.- zzstzooo zzzgz: 33 goz gzk;; ..
    metal naprymsf, chloride. acetopodpide; -; - ЗЗзз; Ззз 5 5 Under sub-; -.i1; zooodl, carbsnilhlord genus /. .sts ns; o zeac: ,, ozlZ S. on mezzy
    From the s used as the primary source podzol, the residual alkali metal iodide salts of the po-tion by pipeline 5 are diverted to a very large value of the iodide 5 Celine reccts and “zr-zrg.z-; however, jacks can be used. and zz; zzyz; In lo.tszszgzyut. Ze- sodium / yurid potassium. In zvezkompress .--. ezzdz. s / evil hplkoztz-pzr E. the cervical organophosphonium-eydzTemparzluzu izkhzdm.kh zzdzztvv by a go-gohm preferring g to use methyltributyl-vz; birz .. h; z ozu-gziokoe t-zplo g / that phosphonium iodide. however, it is also possible55 heating (it is possible to bring the use of other iodides of phosPhone to the reaction temperature of 160-220 ° C. In some cases, for example, etyltriphenylphospho-azoleel vapor-liquid 9 with decomposition of iodide, tetraoutilFos-: Li-iodidress / use heat content or dimethyldirutilsssfynyyodidz. 3isg; ao ots; oyobladz: uchpg; most easy-to-use things 1 and 3 og ozznoa / Ml ievo idih ze; forest.tztoo & ch. ., hl -:
    ldgl1e (gllano) oll; s; ddtelle. .. argument 1 is served in :: j. Julie. ..
    go / h; ; and p .. ,, lll-il.l; -,., .-: -.- - boprszod 13 in the following: d: d, d ;; dd.:. lt-; . Here l is separated, dl - l: ll.-. ..
    MY8 KCA-mOH8i-n; -.,: PD- - hLL:
     i tgkzha submit, r- i - ::.:. . dd.;, t i-ivis co-boilers,. schesgg; and; :: ...
    PICTURE; / ... .Y. ::: -.
    Kachsgve Lubovogs. UO.GU, -,; .-. .;.:. congestion on tru5sg; .ss; od; 4 / пp; , - .. actor 2. B tang. .- b--: - .. substances 12 with; cheerl-i;.; ь, ;; С:.:, ....: ... kokipyuschie aaidestata -.; LJ-.J ,,. L. reacted g e - / P ;-;.:-:: -, through the head of the xyocha -; s. ; Track i return i LU.T, T: H: -
    H - 1H hi.-ioKOx riELi ,,; .-: tdede: :: ... 1iii gas output;.:.: RpySoi.rv.;: -.;, The washer for the exhaust. -E: d washed with cr:; -; th - .., t; ,; substances em laseta,. , .- - ,.:. . cSpaSOiVi or: aoo :: d: d :: g. g ;;.: ..
    H WITH C H /: V; vf- ... S. ,, i ....... . -:
    uruiodooyidu; 7. K, U: .- ..; . ;;;;:. -
    Duration of retirement. , r :; . ..: ..;
    cocroi -t | 1 (.; bL. (G ;; a1.;. x: ..:,.;.,. and acetic acid: -.gd.: /;,: i. -.;;.: 18 idirzy; |;: yut s, .- jr ..-: iv and:
    NW.dBRGS: Sch |. ;TO-; Sl- f-OOr ..: chS.:,: .-. L
    Example, vIOHQCOMSKHOi i - | OL | .3. : .-. -.
    still available saeddo e: - o; ng su - their products yodssodduh ld x .-:; :::,;.
    EUO IS POSSIBLE: E, T: 5: - ::
    haschy salt of silver. /;,; .,. processing both G: Dod, and g:.) -; ... / .-. acid Not sod2 :: zhgshis ,, -.-
    f CO / i DU; D) D wi: L, v. -. .-: -. .
    Noi Dazle K- ;. g li-; .d g .:. that columns 2C gchd.- ;. -lch ..- .. Acid,:, woo: .- n-1., iju y ;;.: ch. .d .; 21 serves i kolsg-d-v 22,, 3 .-: - ..:: for; ,, ,, ..: the golzznuyu part will derive;, p: .-,: ill; -:, dazlen and ist.y uksu. :: ..-::; yy; , g, t
    Time Like H: Sokkdil; LiI4; en OAsv 1:
    vat prsdu kta. ..: /, waters 25,
      р i- i Л Ь у Ј Д1Д) г j И; :: /; ,:; /; l ..
    It is stored at a temperature of 50oa. . .. ... ooem reektora access; s /; lv; i to the mixture of sTerzh t. Dtsisz-. number:; „:,. m 8 v and l t r / i 6 u t and l f o c; about,-; ; / l with: d, d. -. met pacetz e mdl. scil co. ../t 1: 18: 80: 170.
    SSTG.;:, SCHI: l 1 / 1I y it SU O BUT / KIS .. V; j; - .., ZNGIDRIDZ AND ZYSSKOKI-SCH X X Yabi.
    . fijliS- 1: POD / -pT IkO / lO -HirJ. i -.- l U. /. .WITH ./
    ; I will hold 13 gk:; dg; from z zaps /, with:
    .j;: -:; - ;: iy I: and. nni.1 oO C: / ep ..:
     X.G I- 5 N /. JO i-H- H 04 and ,, O: r.if ..: 4; ::. ,.;: Ov 3u "1XC; - t ii fvi: /: .DN: X .Ui i iCri
    Lovy ester As the bottom product of the column 22, 0 05 kg / h of high-boiling substances are removed via line 25. The yield of acetic acid and acetic anhydride per CO used was 98%
    The productivity of the reactor is 1022 g of acetic acid and acetic anhydride / l. Reaction volume per hour. The carbonylation capacity is 556 g. CO / l per reaction volume per hour.
    Examples 3-14 The process is carried out analogously to examples 1 and 2.
    The specific conditions and results of Example 3-10 are given in Table 1, and Examples 11-14 are given in Table 2.
    In the above examples 1-14 hp, the following carbonyl complexes were used:
    a) (CO) or Rh (CO)
    b) (CO) 2 Jz
    c) (CO) 2 J4
    d) Js
    For cases b-2, the corresponding cation is Li (CdHa) C (CH P
    N-CH3
    -V
    //
    4N Formula of the Invention 1 A method of producing acetic acid and acetic anhydride by reacting methanol and methyl acetate with MOHOOKCI carbon or a mixture of carbon monoxide and hydrogen in the presence of a catalytic system containing a carbonyl complex of methyl iodide and an activator — an alkaline methane or an iodine or an iodine — iodine — iodine; organic or ammonium-organic compound in the reaction zone with an increased temperature and pressure of about 1 h and h so that in order to prevent corrosion of methane l and methyl acetate are taken in a molar ratio of 4 64 1-1 8 the interaction is carried out in an anhydrous mixture at a temperature of 160-220 ° C and a pressure of 30-70 bar as the activator of the catalytic system is using lithium iodide acetate methyltributyl phosphonium or iodim N N The dimethylimidazole mixture leaving the reaction zone after carbonylation to convert the dissolved carbon monoxide is passed through an additional reactor at a temperature of 160-220 ° C and a residence time of 2-3 minutes; the pressure leaving the reaction zone at a temperature of 160200 ° C. onno
    0
    0
    WITH
    c / cxs charoioip1 / p i c / -xlt, u JL j zo Rozd L ms o l-Jer (onOn / s, l i 3Tuac ixo xT з t tapalt liquid r and at 01 uL
    for the separation of i-iscock tsv from dap-p ojc pap formed liquid v rei4 L L COST В С i, / 30 J0 p
    015 bar pressure and tempera- ture of 95-145 ° C overtake threso6ps dz, the volatile 1% and to the first ZONE of the diet and quality of health, return from the hospital, with / i r parvl and. diet zone ir pg Ts1% 1 p i f- carbsniliroyanil toar, i
    - Pro - CI with IQOM I H 11 em
    T a and zko / k g i Lei best veins 1 e l l ri (o ia o g g Well, what is your cure Uchsusiog isp / к а ц / i м j i. Ва с
     i o o j i i
    Yu1 tag i g o i i. o o / ant g
     ) /
     About I l bnj1 J P HI P
    1 G G 1 d
    ABOUT
     H (G P t 1
    In 1E SCOI 1G
    Di one IT othhts
    - her veeno 13 g u r g
    6п 1 ОКОМ / l, JHu Ч т-JI, v
    sweep away
    ° t // n And h | 1 Vn) h, - h,
     / axis mgszno z yi rc i e with i-
    F J U / i i
     r2
    g gc i h | a about g / 1che
    hit as quality at ds p thread / bh about c d compound qi xc bdHaL / v nor and / and nickel
    4 Method according to pi i 3 with i / i
    so do you have to do it all right. " be in real 30Hi. in lefL l quantitative yutokie JJL duo for the reaction tone tone cata / i
    l / i NCD OCD-ICT PRODUCTS McTl / i / lLt
    (-1tiAatsegata - nkzhe about and meganols. And mett patsega ta osstl: e min
    5 Method according to PP 14 o i l-i o rf) so that instead of meth la ,. c: tz1y „with,. are di etylov ii sf | /; j
    5 Spsszo on PP 1-L about tl l h yu id and y-, chyu in podpayag / ohm and otsuation zs: -in the answer to the stream, mole p-CHOR cro HOLueH / e, s-d ).,WITH. -Arq /, s., -. g d gztom no A -o Hbdo g, 5tsch | - p 8-2 61 (75-3uj 150-530 psi / Or; j, CrjTpc.L., i-- give birth
      CHL G, 1 O 5 - 1 g-, payment order
      Jo i- olg / t
    7. The way go pg | i-5 distinguishingЈ. Let nos 1-8. about tl, -. W o with "the fact that T1, mg Oo, g; elptch sod
    : I .v., What is the separation of components 10 figtstsv that -o tkgm pz st-Ek svpl:
    , Гь i t ч. LC г, ч (эте
    S, par.-, zora kaal / / zag za. | .Hg, that dist. 11.4tsSh, in .0, mt, l / in the presence of manoox / .da gleosda g-l., .Da carbon, ec, , c, c., jn
    Р Сгог jth пг.-7 о, L- j о and ,, .- with Р T-, I that mixture it. ok .-; h;. / zedusdo up to 5%
    Ј. Let nos 1-8. about tl, -. w y .-,. -. with "the fact that T1, mg Oo, g; elpt,
    c- i
    uh
    (C O
    go
     t
    x
    7
    T. L
    权利要求:
    Claims (6)
    [1]
    Claim
    1. A method of producing acetic acid and acetic anhydride by reacting methanol and methyl acetate with carbon monoxide or a mixture of carbon monoxide and hydrogen in the presence of a catalytic system containing rhodium carbonyl complex, methyl iodide and, as an activator, alkali metal acetate or quaternary phosphonio.organic or organic ammonium iodide compounds in the reaction zone at elevated temperature and pressure, characterized in that, in order to prevent corrosion, methanol and methyl acetate are taken in m the molar ratio of 4.64: 1-1: 8, the interaction is carried out in an anhydrous medium at a temperature of 160-220 ° C and a pressure of 30-70 bar, lithium acetate, methyltributylphosphonium iodide or Ν, Ν-dimethylimidazolium iodide are used as an activator of the catalytic system after carbonylation, the mixture leaving the reaction zone is passed through an additional reactor at 160–220 ° С and residence time to convert dissolved carbon monoxide
    [2]
    2-3 minutes the pressure of the carbonylation reaction mixture leaving the reaction zone at a temperature of 160-200 ° C. is reduced to
    G'-ar in the separation zone is steam liquid. than the bulk of volatile compop. instantly evaporates. and to reduce - 5 drops of liquid through a mist + a feeder · are fed into the first disti zone. · To separate low-boiling combs from the e + / vapor-liquid section formed in the zone and the ac / 10 fog separator in the next target zone. ! ··· With a pressure of 0.15-1 bar and a temperature of · 95-145 ° С, the prevailing volatile components are distilled off and also by throttling: - the first distillation zone, and os + u:. ' the first distillation zone is volatile percent ,, carbonylation by fractional distillation at normal pressure ·, -.
    20 yut on low + otsuyu ¢ + + 47- + ni: + mainly from methyl iodld · lacetate. and returned to the reaction. + +: + well. and as cubic prchdu + h: bees, a mixture of acetic acid and acetic acid: K-. ,
    25 reed. a mixture of acetic acid and anhydride to remove jaedih compounds prs-cheeki /. for salt and salt <- + I process 7 ngduction-protected cho :: about. +
    30 second and third zones dis; and + · ++ -. . pour by way of fra- +++ yy zhuch'ch ... oh komgoneyuk / - /: a // ·; acetic anhydride.
    Method + π 1 about. : and and 7 +. > 35 tech-: what with the first fractions: -h :. and :, <h. 7 in the first zone of D! .io 'il l I tschi from to :. ; l - <- U to exhaust gas. g + s + i-h +; about;. , from Sow. With. HE: / + subtracting ... h ; :. we eat a stream of initial things 7 /; n · -.
    40 methyl acetate. liberate 670 from coo o methyl iodide and direct to. +++ .---. a mixture of methanol and methylacetamate +++ to the + zone.
    [3]
    3. The method according to. 1 and 2. o - and - -
    45 s I that the catalytic 0+ -: -.- 4.
    lives in addition: o asset ”: - CONNECTING ZIRCONIUM, DEPARTMENT. chromium or nickel,
    [4]
    4. The method according to PP. 1-3. from lich Yu.
    50 s, the fact that the residence time is the outcome. · ;; of substances in the reaction zone, depending on the quantity flows, is returned. + ·. into the reaction zone of catalysis ’! u and low-kiln products, methyl iodine + u
    55 methyl acetate, as well as the starting /, proprietary, methanol and methyl acetate. is 9 'min.
    [5]
    5. The method according to PP. 1-4, distinguish w. -> with that one. that instead of methyl acetate isp ·; dimethyl ether.
    about The catalyst solution is carried out. Thus, distillation is carried out in the separation zone in the presence of carbon monoxide or a mixture of carbon monoxide and hydrogen.
    5 8. 1.POSOO on software. - /. ABOUT : /; And x, 3 Yu. Sh., -I / - with the fact that a mixture of monooxldous and hydrogen contains up to 5 about 5% hydrogen.
    [6]
    9. The method of go pl. 1-8. distinguished by the fact that the tumbler separator contains 10 filter cloth made of fiberglass.
    δ. The method according to PP. О-oh. characterized in that the molar ratio between rhodium, activator, in the total quantity of feed supplied to the reaction zone. methyl iododomd.m and 'utyl acetate are maintained equal to i; (1 8-26) :( 78230) :( i 56-580) at a concentration of rhodium C, 008-0.03 mol / L.
    Ί. The method according to PP. Ί-6, characterized in that the separation of volatile components 45 g '· g ί · c s
    Us, w u p J) rib '· i't Syu.'. IsSa::. '<V
    ίyu ίYu ..1. ------ -----g_______ j iF ______ J._3 ί 9 ' 10 Nkhozhl mole ·. CH, OH / · - ' 35 "8 6 36 “2 £ y stings, ΜΛ / '- P well 3 5 Yu well 2Y; YU 2 5 W <.l, C C / h 7 C 0 70.5 " ,5 5' •fifteen 5 . 5 3 1 (- * - to, yes ’-ί / m 8 thirty 25 27.5 29th 32 25 3rd ZUe * ral kϊ - ', ΟςΊ K ·. ·,. L .5ύ .5 3.0 3.0 ό. - • j. ς 3. 5 R . from t Qd,, min ΐ2 23 ιΰ from : L 1 J ; about • al ; ace with so 'g'o ^ sch'ys KI 1 1 Ζ. LtsS AT K.T -. 'Y- 2; - - 'ut.-Mr.-Wo: 2 СО '' m th ; About D met r g - Ζ .. · '‘/ r.-j 30- l. “south, and, - 26• ς :8, well ό ί 3 • about Yu '·· lng-ta l να-Α; - · <.->. - - Yu; e ·; / l- Hexa-g 8 to s a - 7 S.-; al- A - ace-sn · <= · '. ' · - · 8νό,:. + V  about n · l - •••• τ 'e c. ' s < .- / -FROM a ~ 1 L H Όα-ι '· ·'- - - -: M well ZhZ  N. ·· - w yuz ’G 2 '/ 0 'S 2 . s'n'ga. = .: sa. m J-UN 8, 5 99.9 9'8.7 9S, - “8.5 well 99.3 99.8 Дс ^ О-ЗЫДС, СМ / ЛЭй ; - '<3 ~> pCo ~ ΜΛ uh, 2 47.3 98.9 57.2 5 3.0 eg 2 97.3 95.8DIE1U:. U-South., U - '^ choir n mosque ’• Ό With 0 l of hodg;; - /, AZ 98.3 97.7 96.x 96.2 9 7 319 ' ,; W, s Heat- . e v g x.P'Zh.O / g Κν- · “ 1535 •. '·.> h m ’So 2 - * with z ‘7’ f ; ’' '· 1 7 9 • b2 • women x7 “35 658 SW  ·. 3 59 :22 569
    i i UOi-t
    I s
    The introduced mixture is mol. OH, OH / I ml. about l
    Rh / L
    Osoe pOaKi Qpd О · /.
    Duration of stay in the auto
    Ace OH
    Hs> i A
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    同族专利:
    公开号 | 公开日
    NO892882L|1990-01-15|
    CA1339278C|1997-08-12|
    CN1025184C|1994-06-29|
    ES2046375T5|2002-12-16|
    EP0350635B1|1993-09-29|
    ZA895285B|1990-04-25|
    KR900001637A|1990-02-27|
    AU3803789A|1990-01-18|
    US5380929A|1995-01-10|
    EP0350635A1|1990-01-17|
    AU617833B2|1991-12-05|
    NO170539B|1992-07-20|
    DE3823645C1|1989-11-30|
    KR0144154B1|1998-07-15|
    EP0350635B2|2002-07-17|
    NO170539C|1992-10-28|
    NO892882D0|1989-07-12|
    NZ229904A|1991-07-26|
    JPH072672B2|1995-01-18|
    BR8903416A|1990-02-13|
    ES2046375T3|1994-02-01|
    DE58905741D1|1993-11-04|
    AT95158T|1993-10-15|
    JPH02104551A|1990-04-17|
    CN1039410A|1990-02-07|
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    NZ203225A|1982-02-13|1985-01-31|Bp Chem Int Ltd|Coproduction of monocarboxylic acids and anhydrides|
    DE3329781A1|1983-08-18|1985-02-28|Hoechst Ag, 6230 Frankfurt|METHOD FOR SEPARATING IODINE AND ITS COMPOUNDS FROM CARBONYLATION PRODUCTS OBTAINED FROM CARBONYLATING DIMETHYL ETHER, METHYL ACETATE OR METHANOL|
    CA1231965A|1983-12-02|1988-01-26|David J. Schreck|Synergistic production of carboxylic acids fromalcohols|
    DE3429179A1|1984-08-08|1986-02-20|Hoechst Ag, 6230 Frankfurt|METHOD FOR THE SIMULTANEOUS PRODUCTION OF CARBONIC ACIDS AND CARBONIC ACID ANHYDRIDES AND IF ANY. CARBONIC ACID ESTERS|
    DE3429180A1|1984-08-08|1986-02-20|Hoechst Ag, 6230 Frankfurt|METHOD FOR PRODUCING ACETIC ACID ANHYDRIDE AND GGF. ACETIC ACID|
    CA1248549A|1984-08-16|1989-01-10|Richard W. Wegman|Production of anhydrous carboxylic acids fromalcohols using rhodium complex catalysts and organicester source|
    JPH0470245B2†|1984-08-27|1992-11-10|Daicel Chem|
    US4615806B1†|1985-03-07|1994-05-03|Hoechst Co American|Removal of iodide compounds from non-aqueous organic media|
    DE3534070A1|1985-09-25|1987-04-02|Hoechst Ag|METHOD FOR SEPARATING IODINE AND ITS COMPOUNDS FROM CARBONYLATION PRODUCTS OBTAINED FROM CARBONYLATING DIMETHYL ETHER, METHYL ACETATE OR METHANOL|
    JPH0232264B2|1985-09-30|1990-07-19|Hoechst Ag|
    DE3612504A1†|1985-09-30|1987-04-09|Hoechst Ag|METHOD FOR SEPARATING IODINE AND ITS COMPOUNDS FROM CARBONYLATING PRODUCTS CONTAINING CARBBONYLATION OF DIMETHYL ETHER, METHYL ACETATE OR METHANOL|
    US4894477A|1986-10-14|1990-01-16|Hoechst Celanese Corporation|Process for regenerating a carbonylation catalyst solution to remove corrosion metals and carbonylation of methanol to acetic acid|CA1313676C|1987-12-23|1993-02-16|Mark Owen Scates|Purification of acetic acid with ozone|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE3823645A|DE3823645C1|1988-07-13|1988-07-13|
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