NOVELTY - Producing low oxygen biomass-derived pyrolysis oil comprises: contacting carbonaceous biomass feedstock and microporous crystalline zeolitic catalyst at pyrolysis conditions to produce pyrolysis gases comprising hydrocarbons, where catalyst catalyzing deoxygenation reaction converts at least portion of oxygenated hydrocarbons into hydrocarbons and removes oxygen as carbon oxides and water; and condensing a condensable portion of pyrolysis gases. The catalyst comprises microporous crystalline zeolite, UZM-44, having three-dimensional framework of at least alumina and silica tetrahedral units.    USE - The process is useful for producing low oxygen biomass-derived pyrolysis oil (claimed) comprising fully hydrocarbon products which are used for processing into biofuels and chemicals.    ADVANTAGE - The microporous crystalline zeolitic catalyst exhibits: no feature at 200-300 Angstrom on a dV/dlog D versus pore diameter plot of differential volume of nitrogen adsorbed as a function of pore diameter; and an adsorption feature occurring at greater than 450 Angstrom on a dV/dlog D versus pore diameter plot of differential volume of nitrogen adsorbed as a function of pore diameter (all claimed).    DETAILED DESCRIPTION - Producing low oxygen biomass-derived pyrolysis oil, comprises contacting a carbonaceous biomass feedstock with a microporous crystalline zeolitic catalyst at pyrolysis conditions to produce pyrolysis gases comprising hydrocarbons, where the catalyst catalyzing a deoxygenation reaction converts at least a portion of the oxygenated hydrocarbons into hydrocarbons and removes the oxygen as carbon oxides and water; and condensing a condensable portion of the pyrolysis gases to produce low oxygen biomass-derived pyrolysis oil. The catalyst (a) comprises a microporous crystalline zeolite, UZM-44, having a three-dimensional framework of at least alumina and silica tetrahedral units and an empirical composition in synthesized and anhydrous basis expressed by an empirical formula of (NanMm(k+)TtAl1-xExSiyOz) (I), and (b) the microporous crystalline zeolite, UZM-44, where (b) further has the x-ray diffraction pattern having at least the d-spacings and intensities as given in the table A of the specification.    n = mole ratio of Na to (Al+E) and has a value of 0.05-0.5;    M = metal or metals of Zn, group 1, group 2, group 3 and/or lanthanide series of the periodic table;    m = mole ratio of M to (Al+E) and has a value of 0-0.5;    k = average charge of the metal or metals;    M, T = organic structure directing agent or agents derived from reactants R and Q;    R = A, ~o-dihalo substituted alkane having 5C atoms; and    Q = at least one neutral monoamine having 6 or fewer C atoms;    t = mole ratio of N from the organic structure directing agent or agents to (Al+E) and has a value of 0.5-1.5;    E = Ga, Fe, and/or B;    x = E and has a value of 0-1;    y = mole ratio of Si to (Al+E) and has a value greater than 9 to 25; and    z = mole ratio of O to (Al+E) and has a value determined by the equation that z is equal to (n+km+3+4y)/2.