FIELD: chemistry.
SUBSTANCE: catalysts are mixed condensed phosphates, containing (a) at least one anion condensed phosphate of formula (I) [PnO3n+1](n+2)- (I), where n is equal to at least 2, and (b) at least two different cation. Catalyst, in fact, neutral charge, and molar ratio of phosphorus and said at least two different cations is from 0.7 to 1.7. Cations include: (i) at least one univalent cation; and (ii) at least one polyvalent cation, and the multivalent cation is selected from the group consisting of Be2+, Mg2+, Ca2+, Sr2+, Ba2+, Mn2+, Co2+, Ni2+, Cu2+, Zn2+, Cd2+, Sn2+, Pb2+, Ti3+, Cr3+, Mn3+, Al3+, Ga3+, Y3+, In3+, Sb3+, Bi3+, Si4+, Ti4+, V4+, Ge4+, Mo4+, Pt4+, V5+, Nb5+, Sb5+ and mixtures thereof. Invention also discloses methods of producing catalysts. First method comprises steps of mixed and heated at least two different compounds containing phosphor, each said compound is described by one of the formulae (IV) and (XV), or any of hydrated forms said formulae MI y(H3-yPO4) (IV); MII vH(4-2v)P2O7 (XV), where MI represents a univalent cation; where MII is a divalent cation; where y denotes 0, 1, 2 or 3; where v is 0, 1 or 2. Second method comprises steps of mixed and heated (a) at least one compound containing phosphorus, at that each said compound is described by one of the formulae (IV)-(VI) and (XV), or any of hydrated forms said formulae MI y(H3-yPO4) (IV); MII y(H3-yPO4)2 (V); MIII y(H3-yPO4)3 (VI); MII vH(4-2v)P2O7 (XV), where MI represents a univalent cation; where MII is a divalent cation; where MIII is a trivalent cation; where y denotes 0, 1, 2 or 3; where v is 0, 1 or 2; and (b) at least one compound does not contain phosphorus, selected from a group consisting of nitrate salts, at that each said compound is described by one of formulas (XXVI)-(XXVII), or any of hydrated forms said formulae MINO3 (XXVI); MII(NO3)2 (XXVII). Third method comprises steps of (a) Ca2P2O7 and KH2PO4 in molar ratio 3:1 to form a solid mixture, and (b) calcined said solid mixture of stepwise at 50 °C, 80 °C, 120 °C and at from 450 °C to 550 °C, to obtain said catalyst.
EFFECT: there are presented catalysts for dehydration of hydroxipropionic acid derivatives hydroxipropionic acid or mixtures thereof into acrylic acid, acrylic acid derivatives or their mixture with high output and selectivity, short-term stay and without significant conversion in undesirable by-products, such as, for example, acetaldehyde, propionic acid and acetic acid.
24 cl, 2 tbl, 13 ex
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Authors
Dates
2016-07-10—Published
2013-04-11—Filed