A production system for removing impurities from a taurine mother liquor and recovering the taurine mother liquor. The system can be used in an ethylene oxide production process for taurine and the treatment of the last mother liquor of taurine. The system includes, consecutively, an anion resin adsorption device for adsorbing the anions of taurine and sodium isethionate, and an ammonia mixing and desalination device. A feed port of the anion resin adsorption device is operatively connected to receive the last mother liquor of taurine generated in the ethylene oxide taurine production process, and the anion resin adsorption device includes an anion exchange resin column. The ammonia mixing and desalination device includes an ammonia mixing reaction tank, a sealed filtering device, and a circulation path for returning filtrate to the ammonia mixing reaction tank.

A production system for removing impurities from a taurine mother liquor and recovering the taurine mother liquor. The system can be used in an ethylene oxide production process for taurine and the treatment of the last mother liquor of taurine. The system includes, consecutively, an anion resin adsorption device for adsorbing the anions of taurine and sodium isethionate, and an ammonia mixing and desalination device. A feed port of the anion resin adsorption device is operatively connected to receive the last mother liquor of taurine generated in the ethylene oxide taurine production process, and the anion resin adsorption device includes an anion exchange resin column. The ammonia mixing and desalination device includes an ammonia mixing reaction tank, a sealed filtering device, and a circulation path for returning filtrate to the ammonia mixing reaction tank.

A production system for removing impurities from a taurine mother liquor and recovering the taurine mother liquor. The system can be used in an ethylene oxide production process for taurine and the treatment of the last mother liquor of taurine. The system includes, consecutively, an anion resin adsorption device for adsorbing the anions of taurine and sodium isethionate, and an ammonia mixing and desalination device. A feed port of the anion resin adsorption device is operatively connected to receive the last mother liquor of taurine generated in the ethylene oxide taurine production process, and the anion resin adsorption device includes an anion exchange resin column. The ammonia mixing and desalination device includes an ammonia mixing reaction tank, a sealed filtering device, and a circulation path for returning filtrate to the ammonia mixing reaction tank.

The present invention relates to an improved process for the production of alkanesulfonic acids.

The present invention relates to an improved process for the production of alkanesulfonic acids.

The present invention relates to a crystalline form of compound 3-((L-valyl)amino)-3,3-dideuterium-1-propanesulfonic acid, preparation method and uses thereof.

The present invention relates to a crystalline form of compound 3-((L-valyl)amino)-3,3-dideuterium-1-propanesulfonic acid, preparation method and uses thereof.

A method for recovering a distillable, anhydrous methane-sulfonic acid (MSA) liquid phase from an anhydrous 2-phase gas-liquid mixture wherein the anhydrous 2-phase gas-liquid mixture is generated by sulfonating methane (CH.sub.4) with sulfur trioxide (SO.sub.3) in an MSA-forming reactor, or reactor system, according to a radical chain reaction wherein the method comprises (i) separating the gas phase from the liquid phase, (ii) passing the separated liquid phase into a stripping column, and (iii) recovering the stripped anhydrous liquid phase.

A method for recovering a distillable, anhydrous methane-sulfonic acid (MSA) liquid phase from an anhydrous 2-phase gas-liquid mixture wherein the anhydrous 2-phase gas-liquid mixture is generated by sulfonating methane (CH.sub.4) with sulfur trioxide (SO.sub.3) in an MSA-forming reactor, or reactor system, according to a radical chain reaction wherein the method comprises (i) separating the gas phase from the liquid phase, (ii) passing the separated liquid phase into a stripping column, and (iii) recovering the stripped anhydrous liquid phase.

A method for recovering a distillable, anhydrous methane-sulfonic acid (MSA) liquid phase from an anhydrous 2-phase gas-liquid mixture wherein the anhydrous 2-phase gas-liquid mixture is generated by sulfonating methane (CH.sub.4) with sulfur trioxide (SO.sub.3) in an MSA-forming reactor, or reactor system, according to a radical chain reaction wherein the method comprises (i) separating the gas phase from the liquid phase, (ii) passing the separated liquid phase into a stripping column, and (iii) recovering the stripped anhydrous liquid phase.