The present invention includes a composition and process for separating p-isomers of vinylbenzenes from a mixture of isomers comprising the steps of: providing a porous microwaved Mg(II) 2,4-pyridinedicarboxylic acid coordination polymer having a 1-D pore structure and showing reversible soft-crystal behavior by preferentially binding p-isomers of vinylbenzene; adding a mixture of vinylbenzenes isomers to the porous microwaved Mg (II) 2,4-pyridinedicarboxylic acid coordination polymer; adsorbing the p-isomers of vinylbenzene from the mixture of vinylbenzenes isomers; selectively adsorb the p-isomers of vinylbenzene in the 1-D pore structure; removing the mixture of vinylbenzenes isomers; and desorbing the p-isomers of vinylbenzene from the 1-D pore structure to purify the p-isomers of vinylbenzene.

The present invention includes a composition and process for separating p-isomers of vinylbenzenes from a mixture of isomers comprising the steps of: providing a porous microwaved Mg(II) 2,4-pyridinedicarboxylic acid coordination polymer having a 1-D pore structure and showing reversible soft-crystal behavior by preferentially binding p-isomers of vinylbenzene; adding a mixture of vinylbenzenes isomers to the porous microwaved Mg (II) 2,4-pyridinedicarboxylic acid coordination polymer; adsorbing the p-isomers of vinylbenzene from the mixture of vinylbenzenes isomers; selectively adsorb the p-isomers of vinylbenzene in the 1-D pore structure; removing the mixture of vinylbenzenes isomers; and desorbing the p-isomers of vinylbenzene from the 1-D pore structure to purify the p-isomers of vinylbenzene.

The present invention includes a composition and process for separating p-isomers of vinylbenzenes from a mixture of isomers comprising the steps of: providing a porous microwaved Mg(II) 2,4-pyridinedicarboxylic acid coordination polymer having a 1-D pore structure and showing reversible soft-crystal behavior by preferentially binding p-isomers of vinylbenzene; adding a mixture of vinylbenzenes isomers to the porous microwaved Mg (II) 2,4-pyridinedicarboxylic acid coordination polymer; adsorbing the p-isomers of vinylbenzene from the mixture of vinylbenzenes isomers; selectively adsorb the p-isomers of vinylbenzene in the 1-D pore structure; removing the mixture of vinylbenzenes isomers; and desorbing the p-isomers of vinylbenzene from the 1-D pore structure to purify the p-isomers of vinylbenzene.

The present invention relates to a method and gasification system for recycling methane-rich gas from syngas stream emanating from fluidized bed reactor and then returning the methane to the fluidized bed reactor. The method comprises recovering methane-rich gas from the synthesis gas and delivering at least a portion of the recovered methane-rich gas to the fluidized bed reactor. Methods to recover methane-rich gas from syngas at different steps in the gasification system are also provided herein.

The present invention relates to a method and gasification system for recycling methane-rich gas from syngas stream emanating from fluidized bed reactor and then returning the methane to the fluidized bed reactor. The method comprises recovering methane-rich gas from the synthesis gas and delivering at least a portion of the recovered methane-rich gas to the fluidized bed reactor. Methods to recover methane-rich gas from syngas at different steps in the gasification system are also provided herein.

The present invention relates to a method and gasification system for recycling methane-rich gas from syngas stream emanating from fluidized bed reactor and then returning the methane to the fluidized bed reactor. The method comprises recovering methane-rich gas from the synthesis gas and delivering at least a portion of the recovered methane-rich gas to the fluidized bed reactor. Methods to recover methane-rich gas from syngas at different steps in the gasification system are also provided herein.

A method of precipitating polymer and deactivated organometallic catalyst in an olefin oligomerization reaction is provided. The method includes providing an effluent stream from an olefin oligomerization reaction. The effluent stream can include a polymer and an organometallic catalyst. The method can further include introducing sorbent particles into the effluent stream. The sorbent particles can include a deactivating agent. The deactivating agent can be water, an alcohol, an amine, an amino alcohol, or a combination thereof. At least about 10% of the sorbent particles can have a particle size in a range from 10 μm and 60 μm. The method can further include cooling the effluent stream, thereby precipitating polymer and deactivated organometallic catalyst from the effluent stream to provide a precipitate that includes sorbent, polymer, and deactivated catalyst.

A method of precipitating polymer and deactivated organometallic catalyst in an olefin oligomerization reaction is provided. The method includes providing an effluent stream from an olefin oligomerization reaction. The effluent stream can include a polymer and an organometallic catalyst. The method can further include introducing sorbent particles into the effluent stream. The sorbent particles can include a deactivating agent. The deactivating agent can be water, an alcohol, an amine, an amino alcohol, or a combination thereof. At least about 10% of the sorbent particles can have a particle size in a range from 10 μm and 60 μm. The method can further include cooling the effluent stream, thereby precipitating polymer and deactivated organometallic catalyst from the effluent stream to provide a precipitate that includes sorbent, polymer, and deactivated catalyst.

A method of precipitating polymer and deactivated organometallic catalyst in an olefin oligomerization reaction is provided. The method includes providing an effluent stream from an olefin oligomerization reaction. The effluent stream can include a polymer and an organometallic catalyst. The method can further include introducing sorbent particles into the effluent stream. The sorbent particles can include a deactivating agent. The deactivating agent can be water, an alcohol, an amine, an amino alcohol, or a combination thereof. At least about 10% of the sorbent particles can have a particle size in a range from 10 μm and 60 μm. The method can further include cooling the effluent stream, thereby precipitating polymer and deactivated organometallic catalyst from the effluent stream to provide a precipitate that includes sorbent, polymer, and deactivated catalyst.

A method for separating at least one hydrocarbon from a feed containing a mixture of at least one hydrocarbon and nitrogen, comprising contacting the feed with an adsorbent comprising a porous support wherein the porous support comprises exchangeable cations and at least a portion of the exchangeable cations are organic cations.