The use of a composition including at least one acido-basic neutralising agent for decontaminating an atmosphere contaminated by a corrosive gas, the acido-basic neutralising agent having at least 2 pKa's and being characterised by: pKa 1≤pKa 2, pKa 1>2, pKa 2<12, 4<½ (pKa 1+pKa 2)<10 pKa 1, representing the smallest of the basic pKa's and pKa 2 representing the largest of the acidic pKa's. Also, a method for decontaminating an atmosphere contaminated by a corrosive gas comprising the spraying of the neutralising agent, and to a decontamination device.

A solvent system for the removal of acid gases from mixed gas streams is provided. Also provided is a process for removing acid gases from mixed gas streams using the disclosed solvent systems. The solvent systems may be utilized within a gas processing system.

The present invention discloses a desulfurization unit, a solid oxide fuel cell (SOFC) system and a vehicle, the desulfurization unit comprises a container for holding a desulfurizing agent, wherein the container comprises: an inner wall and an outer wall, a water cavity is formed between the inner wall and the outer wall, a water inlet and a water outlet in communication with the water cavity are arranged on the outer wall, the top of the container is provided with a gas outlet and the bottom of the container is provided with a gas inlet; and a double threaded bush arranged at the gas outlet, wherein the double threaded bush comprises an inner bush and an outer bush that adopt threaded connection, the outer wall of the outer bush is connected to the hole wall of the gas outlet in a threaded manner, and the inner wall of the inner bush is connected to an adapter in a threaded manner. The structural design of the desulfurization unit of the SOFC system can effectively solve the problem of slow temperature rise of the desulfurizing agent in the desulfurization unit of the SOFC system.

The present invention discloses a desulfurization unit, a solid oxide fuel cell (SOFC) system and a vehicle, the desulfurization unit comprises a container for holding a desulfurizing agent, wherein the container comprises: an inner wall and an outer wall, a water cavity is formed between the inner wall and the outer wall, a water inlet and a water outlet in communication with the water cavity are arranged on the outer wall, the top of the container is provided with a gas outlet and the bottom of the container is provided with a gas inlet; and a double threaded bush arranged at the gas outlet, wherein the double threaded bush comprises an inner bush and an outer bush that adopt threaded connection, the outer wall of the outer bush is connected to the hole wall of the gas outlet in a threaded manner, and the inner wall of the inner bush is connected to an adapter in a threaded manner. The structural design of the desulfurization unit of the SOFC system can effectively solve the problem of slow temperature rise of the desulfurizing agent in the desulfurization unit of the SOFC system.

An installation for the production of oil, gas and char for carbon black, from elastomers, characterized in that, it has a screw dispenser (3) with a shaft (1), which from the loading side is closed hydraulically with a lock (2) by a nitrogen, a reactor (4), which is divided into zones A, B, C, corresponding to the subsequent stages of the pyrolysis process: zone A—the beginning of depolymerization (350° C.), zone B—carbonization (350-400° C.) and zone C—aromatic compounds cracking (400-650° C.), while a bubbler (5) hydraulically closed with a siphon (6) and a separator (7) with a hydraulic closure (8) and an oil separator (9) equipped with a transport screw (10) and an afterburner chamber (20) are installed outside the reactor (4), wherein the oil separator (9) is closed at the outlet by an accumulation shaft (12) and from the side of receiving a solid product—with a shaft (13), which is connected by an U-shaped screw conveyor (14) with economizers (11) and (15). wherein the installation is provided with a scrubber (16).

An installation for the production of oil, gas and char for carbon black, from elastomers, characterized in that, it has a screw dispenser (3) with a shaft (1), which from the loading side is closed hydraulically with a lock (2) by a nitrogen, a reactor (4), which is divided into zones A, B, C, corresponding to the subsequent stages of the pyrolysis process: zone A—the beginning of depolymerization (350° C.), zone B—carbonization (350-400° C.) and zone C—aromatic compounds cracking (400-650° C.), while a bubbler (5) hydraulically closed with a siphon (6) and a separator (7) with a hydraulic closure (8) and an oil separator (9) equipped with a transport screw (10) and an afterburner chamber (20) are installed outside the reactor (4), wherein the oil separator (9) is closed at the outlet by an accumulation shaft (12) and from the side of receiving a solid product—with a shaft (13), which is connected by an U-shaped screw conveyor (14) with economizers (11) and (15). wherein the installation is provided with a scrubber (16).

An integrated wellhead device for filtering injected and produced gases is provided by the present disclosure, comprising a horizontal tank body that is internally provided with an injected gas filtering system and a produced gas filtering system, wherein the injected gas filtering system is internally provided with an oxygen removal chamber, the gas inlet of the injected gas filtering system is connected with an injected high-pressure gas source, and the gas outlet of the injected gas filtering system is connected with a gas injection well casing of Christmas tree, the produced gas filtering system is internally equipped with an oxygen removal chamber, a sulfur removal chamber and a carbon dioxide removal chamber, the gas inlet of the produced gas filtering system is connected with a gas production tubing of the Christmas tree, and the gas outlet of the produced gas filtering system is connected with a produced gas transmission pipe.

An integrated wellhead device for filtering injected and produced gases is provided by the present disclosure, comprising a horizontal tank body that is internally provided with an injected gas filtering system and a produced gas filtering system, wherein the injected gas filtering system is internally provided with an oxygen removal chamber, the gas inlet of the injected gas filtering system is connected with an injected high-pressure gas source, and the gas outlet of the injected gas filtering system is connected with a gas injection well casing of Christmas tree, the produced gas filtering system is internally equipped with an oxygen removal chamber, a sulfur removal chamber and a carbon dioxide removal chamber, the gas inlet of the produced gas filtering system is connected with a gas production tubing of the Christmas tree, and the gas outlet of the produced gas filtering system is connected with a produced gas transmission pipe.

An apparatus and methods to eliminate PFAS from wastewater biosolids through fluidized bed gasification. The gasifier decomposes the PFAS in the biosolids at temperatures of 900-1800° F. Synthesis gas (syngas) exits the gasifier which is coupled to a thermal oxidizer and is combusted at temperatures of 1600-2600° F. This decomposes PFAS in the syngas and creates flue gas. Heat can be recovered from the flue gas by cooling the flue gas to temperatures of 400-1200° F. in a heat exchanger that is coupled with the thermal oxidizer. Cooled flue gas is mixed with hydrated lime, enhancing PFAS decomposition, with the spent lime filtered from the cooled flue gas using a filter system that may incorporate catalyst impregnated filter elements. The apparatus and methods thereby eliminate PFAS from wastewater biosolids and control emissions in the resulting flue gas.

An apparatus and methods to eliminate PFAS from wastewater biosolids through fluidized bed gasification. The gasifier decomposes the PFAS in the biosolids at temperatures of 900-1800° F. Synthesis gas (syngas) exits the gasifier which is coupled to a thermal oxidizer and is combusted at temperatures of 1600-2600° F. This decomposes PFAS in the syngas and creates flue gas. Heat can be recovered from the flue gas by cooling the flue gas to temperatures of 400-1200° F. in a heat exchanger that is coupled with the thermal oxidizer. Cooled flue gas is mixed with hydrated lime, enhancing PFAS decomposition, with the spent lime filtered from the cooled flue gas using a filter system that may incorporate catalyst impregnated filter elements. The apparatus and methods thereby eliminate PFAS from wastewater biosolids and control emissions in the resulting flue gas.