Disclosed herein is a method comprising the steps of: a) producing a hydrocarbon stream from syngas via a Fischer-Tropsch reaction, wherein the hydrocarbon stream comprises a first C2 hydrocarbon stream comprising ethane and a first ethylene product; b) separating at least a portion of the first C2 hydrocarbon stream from the hydrocarbon stream; c) separating at least a portion of the first ethylene product from the first C2 hydrocarbon stream, thereby producing a second C2 hydrocarbon stream; d) converting at least a portion of the ethane in the second C2 hydrocarbon stream to a second ethylene product; and e) producing ethylene oxide from at least a portion of the second ethylene product.

Disclosed herein is a method comprising the steps of: a) producing a hydrocarbon stream from syngas via a Fischer-Tropsch reaction, wherein the hydrocarbon stream comprises a first C2 hydrocarbon stream comprising ethane and a first ethylene product; b) separating at least a portion of the first C2 hydrocarbon stream from the hydrocarbon stream; c) separating at least a portion of the first ethylene product from the first C2 hydrocarbon stream, thereby producing a second C2 hydrocarbon stream; d) converting at least a portion of the ethane in the second C2 hydrocarbon stream to a second ethylene product; and e) producing ethylene oxide from at least a portion of the second ethylene product.

A conditioning process that is employed with a high selectivity catalyst (HSC) during an initial phase (i.e., start-up) of the epoxidation process is provided. The HSC conditioning process of the present disclosure ensures that the heat release from a catalyst bed containing an HSC during a start-up operation is less than 2000 kJ/Kgcat.Math.hr. The HSC containing catalyst bed that has been conditioned by the process of the present disclosure exhibits improved performance (i.e., EO selectivity) and reduced hot spots.

A process for the epoxidation of ethylene comprising: contacting an inlet feed gas comprising ethylene, oxygen and one or more reaction modifiers consisting of organic chlorides with an epoxidation catalyst comprising a carrier, and having silver, a rhenium promoter, and one or more alkali metal promoters deposited thereon; wherein the inlet feed gas has an overall catalystchloriding effectiveness value (Cleff) represented by the formula (I): wherein [MC], [EC], [EDC], and [VC] are the concentrations in ppmv of methyl chloride (MC), ethylchloride (EC), ethylene dichloride (EDC), and vinylchloride (VC), respectively, and [CH.sub.4], [C.sub.2H.sub.6] and [C.sub.2H.sub.4] are the concentrations in mole percent of methane, ethane, and ethylene, respectively, in the inlet feedgas; wherein at a cumulative ethylene oxide production cumEO.sub.1 of at least 0.2 kton ethylene oxide/m.sup.3 catalyst, said process is operating at a reaction temperature having a value T.sub.1 and with the inlet feed gas having an optimum overall catalyst chloriding effectiveness value of Cl.sub.eff1 to produce ethylene oxide with an ethylene oxide production parameter at a value EO.sub.1; and characterised in that the carrier is a fluoride-mineralized alpha-alumina carrier and said process is subsequently operated such that at a cumulative ethylene oxide production cumEO.sub.x, wherein cumEO.sub.x is at least 0.6 kton ethylene oxide/m.sup.3 catalyst greater than cumEO.sub.1, the reaction temperature 5 has an increased value T.sub.x to maintain said ethylene oxide production parameter at a value EO1 whilst the optimum overall catalyst chloriding effectiveness value of the inlet feed gas Cl.sub.effx is controlled such that the ratio of Cl.sub.effx/Cl.sub.eff1 is in the range of from 0.8 to 1.2.

[00001]

A process for the epoxidation of ethylene comprising: contacting an inlet feed gas comprising ethylene, oxygen and one or more reaction modifiers consisting of organic chlorides with an epoxidation catalyst comprising a carrier, and having silver, a rhenium promoter, and one or more alkali metal promoters deposited thereon; wherein the inlet feed gas has an overall catalystchloriding effectiveness value (Cleff) represented by the formula (I): wherein [MC], [EC], [EDC], and [VC] are the concentrations in ppmv of methyl chloride (MC), ethylchloride (EC), ethylene dichloride (EDC), and vinylchloride (VC), respectively, and [CH.sub.4], [C.sub.2H.sub.6] and [C.sub.2H.sub.4] are the concentrations in mole percent of methane, ethane, and ethylene, respectively, in the inlet feedgas; wherein at a cumulative ethylene oxide production cumEO.sub.1 of at least 0.2 kton ethylene oxide/m.sup.3 catalyst, said process is operating at a reaction temperature having a value T.sub.1 and with the inlet feed gas having an optimum overall catalyst chloriding effectiveness value of Cl.sub.eff1 to produce ethylene oxide with an ethylene oxide production parameter at a value EO.sub.1; and characterised in that the carrier is a fluoride-mineralized alpha-alumina carrier and said process is subsequently operated such that at a cumulative ethylene oxide production cumEO.sub.x, wherein cumEO.sub.x is at least 0.6 kton ethylene oxide/m.sup.3 catalyst greater than cumEO.sub.1, the reaction temperature 5 has an increased value T.sub.x to maintain said ethylene oxide production parameter at a value EO1 whilst the optimum overall catalyst chloriding effectiveness value of the inlet feed gas Cl.sub.effx is controlled such that the ratio of Cl.sub.effx/Cl.sub.eff1 is in the range of from 0.8 to 1.2.

[00001]

Disclosed is a method for preparing a material of plant origin rich in phenolic acids, including at least one metal, including: preparing a material of plant origin chosen from: aquatic plants; materials rich in tannins; materials rich in lignin; and obtaining a material of plant origin, rich in phenolic acids, in which the ratio of the intensity of the vibration band of the CO bond of the COOH group and the intensity of each of the vibration bands the aromatic ring determined in FT-IR is between 0.5 and 4. The material of plant origin is brought into contact with an effluent including from 0.1 to 1000 mg/l of at least one metal, thus obtaining a material of plant origin rich in phenolic acids including from 1 to 30% by weight of at least one metal relative to the total weight of the material.

The object of the present invention is to provide a process for preparing a 5-alken-1-yne compound efficiently at low costs and a process for preparing (2E,6Z)-2,6-nonadienal by making use of the aforesaid process for preparing the 5-alken-1-yne compound.

There is provided a process for preparing a 5-alken-1-yne compound of the following formula (4): Y-Z-CR.sup.1CR.sup.2(CH.sub.2).sub.2CCH (4) in which Y in formula (4) represents a hydrogen atom or a hydroxyl group, the process comprising at least steps of: subjecting (i) an alkenylmagnesium halide compound prepared from a haloalkene compound of the following formula (1): Y-Z-CR.sup.1CR.sup.2(CH.sub.2).sub.2-X.sup.1 (1) and (ii) an alkyne compound of the following formula (2): X.sup.2=CCSi(R.sup.3)(R.sup.4)(R.sup.5) (2) to a coupling reaction to form a silane compound of the following formula (3): Y-Z-CR.sup.1CR.sup.2(CH.sub.2).sub.2CCSi(R.sup.3)(R.sup.4)(R.sup.5) (3); and subjecting the silane compound (3) to a desilylation reaction to form the 5-alken-1-yne compound (4).

The object of the present invention is to provide a process for preparing a 5-alken-1-yne compound efficiently at low costs and a process for preparing (2E,6Z)-2,6-nonadienal by making use of the aforesaid process for preparing the 5-alken-1-yne compound.

There is provided a process for preparing a 5-alken-1-yne compound of the following formula (4): Y-Z-CR.sup.1CR.sup.2(CH.sub.2).sub.2CCH (4) in which Y in formula (4) represents a hydrogen atom or a hydroxyl group, the process comprising at least steps of: subjecting (i) an alkenylmagnesium halide compound prepared from a haloalkene compound of the following formula (1): Y-Z-CR.sup.1CR.sup.2(CH.sub.2).sub.2-X.sup.1 (1) and (ii) an alkyne compound of the following formula (2): X.sup.2=CCSi(R.sup.3)(R.sup.4)(R.sup.5) (2) to a coupling reaction to form a silane compound of the following formula (3): Y-Z-CR.sup.1CR.sup.2(CH.sub.2).sub.2CCSi(R.sup.3)(R.sup.4)(R.sup.5) (3); and subjecting the silane compound (3) to a desilylation reaction to form the 5-alken-1-yne compound (4).

Disclosed is a method for preparing a solid material including manganese, the method including the following steps: a. bringing into contact an aqueous effluent including manganese, for example at least 5 mg/L, typically at least 5 to 50 mg/L, and preferably 7 to 25 mg/L of manganese, with an oxidizing agent, manganese, preferably at a temperature between 10 C. and 50 C., and obtaining an oxidized aqueous solution; b. adding a base to the oxidized aqueous solution obtained at the end of step a) until a pH of between 8 and 12, preferably greater than 9, and preferably from 9 to 10.5, and obtaining a solution including a precipitate; c. filtration of the solution obtained at the end of step b); and d. obtaining a solid material including manganese, and especially manganese (IV) and/or Mn (III).

An ethylene bis-12-hydroxystearamide grafted glycidyl citrate (EBH-g-ECA) and a preparation method thereof are provided; the EBH-g-ECA can be used as a multifunctional auxiliary agent in a polymer material, and particularly has a chain extension and a crystal nucleation effect in a polyester polymer material. A heat-resistant polylactic acid continuously-extruded foamed material containing EBH-g-ECA is further provided. The continuous foaming technology can be realized by using the heat-resistant polylactic acid foamed material, and the prepared foamed product has a high heat resistance, a uniform appearance, a low density, and complete biodegradation. A polylactic acid foamed material preparation method for a heat-resistant is provided, which is easy to be industrialized and has a great significance for realizing the large-scale replacement of petroleum-based plastic disposable foamed products such as PP and PS.