首页> 外国专利> PROCESS FOR ALDEHYDE BYPRODUCT REDUCTION IN ACRYLIC ACID PRODUCTION USING HIGHLY ACTIVE AND SELECTIVE CATALYSTS

PROCESS FOR ALDEHYDE BYPRODUCT REDUCTION IN ACRYLIC ACID PRODUCTION USING HIGHLY ACTIVE AND SELECTIVE CATALYSTS

机译:高活性和选择性催化剂在丙烯酸生产中醛副产物的还原过程

摘要

A catalyst composition comprises an acrolein-oxidizing catalyst comprising a mixed metal oxide catalyst of general formula (I): MoVaA1bA2cA3dOm in which A1 comprises at least one element selected from the group consisting of W and Cu; A2 comprises at least one element selected from the group consisting of Sb, Fe, and Nb; A3 comprises at least one element selected from the group consisting of Y, Ti, Zr, Hf, Ta, Cr, Mn, Re, Ru, Co, Rh, Ir, Ni, Pd, Pt, Ag, Au, Zn, B, Al, Ga, In, Ge, Sn, Si, Te, Pb, P, As, Bi, Se, rare earth elements, alkaline elements, and alkaline earth elements; a ranges from 0.01 to 1.0; b ranges from 0.01 to 1.5; c ranges from 0 to 1.5; d ranges from 0 to 1.0; and m is dependent on the oxidation state of the other elements. The catalyst composition further comprises a finishing catalyst comprising a mixed metal oxide catalyst of general formula (II): MoVwNbxX1y X2zOn in which X1 comprises at least one element selected from the group consisting of Te and Sb; X2 comprises at least one an element selected from the group consisting of Y, Ti, Zr, Hf, Nb, Ta, Cr, Mn, Re, Fe, Ru, Co, Rh, Ir, Ni, Pd, Pt, Ag, Au, Zn, B, Al, Ga, In, Ge, Sn, Pb, P, As, Bi, Se, rare earth elements and alkaline earth elements; w ranges from 0.01 to 1.0; x ranges from 0.01 to 1.0; y ranges from 0.01 to 1.0; z ranges from 0 to 1.0; and n is depended on the oxidation state of the other elements. The finishing catalyst does not contain W or Cu, and has an X-ray diffraction pattern showing an orthorhombic phase as the major crystal phase with main peaks with 2θ at 6.7°, 7.8°, 22.1°, and 27.2°. The acrolein-oxidizing catalyst has a different chemical composition than the finishing catalyst. A process for producing acrylic acid is also disclosed.
机译:催化剂组合物包含丙烯醛氧化催化剂,所述丙烯醛氧化催化剂包含通式(I)的混合金属氧化物催化剂:MoV a A 1 b A < Sup> 2 c A 3 d O m 其中A 1 包括选自由W和Cu组成的组中的至少一种元素;和A 2 包含选自由Sb,Fe和Nb组成的组中的至少一种元素。 A 3 包含至少一种选自以下元素的元素:Y,Ti,Zr,Hf,Ta,Cr,Mn,Re,Ru,Co,Rh,Ir,Ni,Pd,Pt, Ag,Au,Zn,B,Al,Ga,In,Ge,Sn,Si,Te,Pb,P,As,Bi,Se,稀土元素,碱金属元素和碱土金属元素; a的范围从0.01到1.0; b的范围为0.01至1.5; c为0至1.5; d的范围是0到1.0; m取决于其他元素的氧化态。该催化剂组合物还包含整理催化剂,该整理催化剂包含通式(II)的混合金属氧化物催化剂:MoV w Nb x X 1 y X 2 z O n 其中X 1 包含至少一个元素由Te和Sb组成的组; X 2 包括至少一种选自Y,Ti,Zr,Hf,Nb,Ta,Cr,Mn,Re,Fe,Ru,Co,Rh,Ir,Ni的元素,Pd,Pt,Ag,Au,Zn,B,Al,Ga,In,Ge,Sn,Pb,P,As,Bi,Se,稀土元素和碱土元素; w范围为0.01至1.0; x范围为0.01至1.0; y的范围为0.01到1.0; z的范围是0到1.0; n取决于其他元素的氧化态。精加工催化剂不包含W或Cu,并且具有X射线衍射图,该图显示出正交晶相作为主晶相,主峰在6.7°,7.8°,22.1°和27.2°具有2θ。丙烯醛氧化催化剂具有与整理催化剂不同的化学组成。还公开了一种生产丙烯酸的方法。

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