A method for recovering dimethyl sulfoxide, including a step of contacting a recovered resist remover containing at least one compound selected from the group consisting of glycol ether, glycol and triol, and dimethyl sulfoxide with water and performing distillation.

Ethylene oxide purification by quenching and washing ethylene oxide reactor effluent prior to passing the gaseous ethylene oxide-containing stream to an ethylene oxide absorber to form a dilute aqueous ethylene oxide and carbon dioxide solution and thereafter stripping that solution in an EO stripper to produce a gaseous ethylene oxide and carbon dioxide-containing overhead vapor which is then passed to a reabsorber wherein the ethylene oxide and part of the carbon dioxide vapors are absorbed to form an aqueous reabsorbate solution from which carbon dioxide is removed to produce an ethylene oxide-containing solution is improved by passing an impurities-containing liquid bleed stream obtained from the quench wash to a second, small quench bleed stripper where steam and carbon dioxide are added and gaseous overhead from that quench bleed stripper is passed to the reabsorber for recovery of the EO and removal of formaldehyde and other impurities.

Ethylene oxide purification by quenching and washing ethylene oxide reactor effluent prior to passing the gaseous ethylene oxide-containing stream to an ethylene oxide absorber to form a dilute aqueous ethylene oxide and carbon dioxide solution and thereafter stripping that solution in an EO stripper to produce a gaseous ethylene oxide and carbon dioxide-containing overhead vapor which is then passed to a reabsorber wherein the ethylene oxide and part of the carbon dioxide vapors are absorbed to form an aqueous reabsorbate solution from which carbon dioxide is removed to produce an ethylene oxide-containing solution is improved by passing an impurities-containing liquid bleed stream obtained from the quench wash to a second, small quench bleed stripper where steam and carbon dioxide are added and gaseous overhead from that quench bleed stripper is passed to the reabsorber for recovery of the EO and removal of formaldehyde and other impurities.

The present disclosure relates to a system and a method for continuously purifying a reaction product of esterification, where the system includes a neutralizer, a distiller, and a product purifier. Through the present system and the method, it is possible to perform a continuous purification process efficiently, and to reduce lower alcohol wastewater generated during purification.

The present disclosure relates to a system and a method for continuously purifying a reaction product of esterification, where the system includes a neutralizer, a distiller, and a product purifier. Through the present system and the method, it is possible to perform a continuous purification process efficiently, and to reduce lower alcohol wastewater generated during purification.

A method for extracting and isolating terpenes and aromatic compounds from Cannabis plant material by the steps of grinding the cannabis plant material to obtain a ground cannabis, performing a CO2 supercritical extraction upon a first portion of the ground cannabis, wherein said supercritical extraction is performed at temperature below freezing, between −30 to 0 centigrade, for a period of 3 to 5 hours, at between 1000-1300 psi, performing a steam distillation upon a second portion of the ground cannabis, performing a butane extraction upon a third portion of the ground cannabis, wherein the butane extraction is performed at a temperature between −30 to 0 centigrade, performing an alcohol extraction upon a fourth portion of the ground cannabis, wherein the alcohol extraction is performed at a temperature between −30 to 0 centigrade, performing a maceration upon a fifth portion of the ground cannabis, wherein the maceration is performed with coconut oil at a temperature of between 40-70 centigrade, combining at least a portion of each of the resultant extracts from the CO2 supercritical extraction step, the steam distillation step, the butane extraction step, the alcohol extraction step and the maceration step to create a combined extract, and then fractionally distilling the combined extract to separate terpenes and other aromatic compounds from the combined extract.

A method for extracting and isolating terpenes and aromatic compounds from Cannabis plant material by the steps of grinding the cannabis plant material to obtain a ground cannabis, performing a CO2 supercritical extraction upon a first portion of the ground cannabis, wherein said supercritical extraction is performed at temperature below freezing, between −30 to 0 centigrade, for a period of 3 to 5 hours, at between 1000-1300 psi, performing a steam distillation upon a second portion of the ground cannabis, performing a butane extraction upon a third portion of the ground cannabis, wherein the butane extraction is performed at a temperature between −30 to 0 centigrade, performing an alcohol extraction upon a fourth portion of the ground cannabis, wherein the alcohol extraction is performed at a temperature between −30 to 0 centigrade, performing a maceration upon a fifth portion of the ground cannabis, wherein the maceration is performed with coconut oil at a temperature of between 40-70 centigrade, combining at least a portion of each of the resultant extracts from the CO2 supercritical extraction step, the steam distillation step, the butane extraction step, the alcohol extraction step and the maceration step to create a combined extract, and then fractionally distilling the combined extract to separate terpenes and other aromatic compounds from the combined extract.

A method and system for rapidly preparing lithium carbonate or concentrated brine using high-temperature steam. The method comprises the steps of: feeding brine into a reactor, heating the brine with high-temperature steam above 200° C. while simultaneously discharging steam produced in the reactor, cooling and condensing the discharged steam in a condenser and collecting the condensate, and stopping the high-temperature steam after the brine is concentrated to a predetermined concentration or after a sufficient amount of lithium carbonate is collected. The system comprises: a reactor provided with a brine inlet, a steam outlet connected to a condenser, a product outlet, and a plurality of steam pipes. The method concerns the direct heating of brine using high-temperature steam, which is effective and efficient, and also produces fresh water. The heating is uniform and rapid, and does not require jackets, heat exchange tubes, mixers and vacuum pumps, vastly simplifying the system.

A method and system for rapidly preparing lithium carbonate or concentrated brine using high-temperature steam. The method comprises the steps of: feeding brine into a reactor, heating the brine with high-temperature steam above 200° C. while simultaneously discharging steam produced in the reactor, cooling and condensing the discharged steam in a condenser and collecting the condensate, and stopping the high-temperature steam after the brine is concentrated to a predetermined concentration or after a sufficient amount of lithium carbonate is collected. The system comprises: a reactor provided with a brine inlet, a steam outlet connected to a condenser, a product outlet, and a plurality of steam pipes. The method concerns the direct heating of brine using high-temperature steam, which is effective and efficient, and also produces fresh water. The heating is uniform and rapid, and does not require jackets, heat exchange tubes, mixers and vacuum pumps, vastly simplifying the system.

A process for producing valuable aromatic hydrocarbons from a crude or semi-crude shale gas stream. A crude or semi-crude shale gas stream including methane is introduced into a reactor that converts at least a portion of the ethane component into aromatic hydrocarbons. Unreacted methane, other hydrocarbons, and hydrogen may then be easily separated from the aromatic hydrocarbons. Because methane is not separated from the shale gas stream, the expensive and resource-consuming shale gas C1/C2+ separation step is avoided.