Abstract:
A high-silica content zeolite having a novel crystal structure, a zeolite membrane and manufacturing methods for these are provided, and the present invention relates to a zeolite having the chemical composition represented by [(Si36-xTy.O72).Mz] (wherein M is a cation of an alkali metal such as Li, Na, K or Rb, T represents Al, Ga, Fe and Ce as skeleton substituting elements, x satisfies 0≦x≦3.0, y satisfies 0≦y≦1.0 and z satisfies 0≦z≦3.0), and having a micropore formed of covalent bonds between Si and O atoms, with a specific diffraction peak at 2θ in powder x-ray diffraction, together with a zeolite membrane and methods for manufacturing these.
Abstract translation:提供了具有新型晶体结构的高二氧化硅含量沸石,沸石膜及其制造方法,本发明涉及具有由[(Si u> (其中M是碱金属如Li,Na,K或Rb的阳离子)(其中M是碱金属的阳离子,例如Li,Na,K或Rb ,T表示Al,Ga,Fe和Ce作为骨架取代元素,x满足0 <= x <= 3.0,y满足0 <= y <= 1.0,z满足0 <= z <= 3.0),并具有微孔 由Si和O原子之间的共价键形成,在粉末x射线衍射中在2θ处具有特定衍射峰,以及沸石膜及其制造方法。
Abstract:
The invention relates to a process for preparing caprolactam by admixture of cyclohexanone oxime to a reaction mixture comprising caprolactam and sulfuric acid using a mixing device, said mixing device comprising (i) a tube through which the reaction mixture can flow, and (ii) channels disposed around the tube, said channels opening into the tube, said process comprising: passing the reaction mixture through the tube, and feeding the cyclohexanone oxime into the reaction mixture through one or more of said channels, wherein Re>5000, Re being the Reynolds number as defined by ρ·V·D/η, wherein ρ=density (in kg/m3) of the reaction mixture that is fed to the tube V=velocity of the reaction mixture, V being defined as W/A, wherein W is the flow rate (in m3/s) of the reaction mixture that is fed into the tube and A is the cross section area of the tube (in m2) at the level where said channels open into the tube D=diameter of the tube at the level where said channels open into the tube (in m) η=viscosity of the reaction mixture that is fed into the tube (in Pa·s).
Abstract translation:本发明涉及通过使用混合装置将环己酮肟与包含己内酰胺和硫酸的反应混合物混合来制备己内酰胺的方法,所述混合装置包括(i)反应混合物可以流过的管,以及(ii)通道 所述方法包括:使反应混合物通过管,并通过一个或多个所述通道将环己酮肟进料到反应混合物中,其中Re> 5000,Re为雷诺数 其数值由rho.VD / eta定义,其中rho =加入到管中的反应混合物的密度(单位为kg / m 3)V =反应混合物的速度,V定义为 W / A,其中W是供给到管中的反应混合物的流速(以m 3 S / s),A为管的横截面积(m / 2)在所述通道打开到管中的水平面D =在其上的管的直径 所述通道通入管中(以m计)eta =进料到管中的反应混合物的粘度(Pa.s)。
Abstract:
Disclosed are a kenyaite catalyst containing a metal oxide between layers of a layered silicate having kenyaite structure, a method for preparing the same, and a method for preparing ε-caprolactam from cyclohexanone oxime by applying the catalyst to gas phase Beckmann rearrangement.
Abstract:
ε-Caprolactam is produced by contacting cyclohexanone oxime with a solid acid catalyst in the gaseous phase to effect a rearrangement reaction of the cyclohexanone oxime. The solid acid catalyst is produced by calcining a dried catalyst precursor that can be a zeolite, a crystalline clay mineral and at least one substance selected from an inorganic oxide and a compound which forms the inorganic oxide by calcination. The inorganic oxide includes at least one element selected Groups 4, 13 and 14 of the Periodic Table, and the inorganic oxide excludes oxides contained in a crystalline form in the zeolite and the crystalline clay mineral. Alternately, the rearrangement reaction occurs in the presence of a polyhydric alcohol compound R1—O—R2—OH (where R1 represents C1-C5 alkyl or phenyl, and R2 represents C2-C5 alkylene).
Abstract:
The present invention provides a method for producing .epsilon.-caprolactam, which comprises subjecting cyclohexene to a hydration reaction to obtain cyclohexanol, subjecting the cyclohexanol to a dehydrogenation reaction to obtain cyclohexanone, subjecting the cyclohexanone to an oxime-forming reaction to obtain cyclohexanone oxime, and subjecting the cyclohexanone oxime to a Beckmann rearrangement reaction to obtain .epsilon.-caprolactam, wherein methylcyclopentanones contained in the cyclohexanone subjected to the oxime-forming reaction are controlled to be not more than 400 ppm.According to the present invention, it is possible to produce .epsilon.-caprolactam having a quality not inferior to conventional quality at a low cost.
Abstract:
A process for the preparation of caprolactam by reacting cyclohexanone oxime with a cationic or nonionic surfactant and a cosurfactant in dilute sulfuric acid at a temperature in the range of 15.degree. C. to 40.degree. C., neutralizing excess acid present in the solution and recovering the caprolactam from the solution by filtration.
Abstract:
.epsilon.-Caprolactam is prepared by subjecting cyclohexanone oxime in a gas phase to a catalytic reaction using zeolite catalysts in the presence of water and at least one compound selected from alcohols and ether compounds.
Abstract:
A process is provided for catalytically converting cyclohexanone oxime to epsilon caprolactam. The conversion is characterized by exceptionally high selectivity and reduced rate of catalyst aging, even at single pass conversion above 90 percent. The conversion catalyst is a medium pore size crystalline zeolite exemplified by ZSM-5 which has low acid activity. Recycling unconverted oxime provides excellent ultimate yield of caprolactam.
Abstract:
A process for the catalyzed conversion of oximes such as cyclohexanone oxime to amides such as caprolactam via a high conversion, high selectivity, long catalyst lifetime reaction over a HAMS-1B crystalline borosilicate-based catalyst composition.