Abstract:
An improved reactor for an HF alkylation unit of the shell-and-tube heat exchanger type has an axial tube bundle to provide cooling for the reactor and a centrally-located axial sparger system for injecting and dispersing the hydrocarbon reactants into the flow path in the reactor. The sparger comprises an axially-extensive tube with outlet nozzles for the hydrocarbon reactants arranged around the tube, preferably with differing radial angles, at different locations along the length of the sparger.
Abstract:
An apparatus is provided to generate a gas by mixing chemicals with water. Typically, the production of gas, particularly oxygen, by combining water with powders and other dry chemicals has not been widely employed. There have existed a number of preexisting barriers such as undesirable flow rates and yields. However, by utilizing multiple reaction chambers the flow rates and yields can be more precisely tailored for a variety of situations that may call for particular flow rates and yields. Additionally, the use of the dry chemicals would allow for a long self-life allowing the apparatus to be particularly useful in emergency situations.
Abstract:
A gas removal system that removes a halogen gas remaining inside a processing chamber after executing a specific type of processing inside the processing chamber maintained in an airtight state with plasma obtained through discharge dissociation of the halogen gas supplied from a gas supply device comprises a pressure control device that controls the pressure inside the processing chamber, an air supply device that supplies the atmospheric air into the processing chamber after the pressure inside the processing chamber is lowered by the pressure control device, a control device that controls the air supply device and an evacuation device that evacuates a gas produced through a reaction of the halogen gas and the atmospheric air having occurred inside the processing chamber.
Abstract:
An apparatus is provided to generate a gas by mixing chemicals with water. Typically, the production of gas, particularly oxygen, by combining water with powders and other dry chemicals has not been widely employed. There have existed a number of preexisting barriers such as undesirable flow rates and yields. However, by utilizing multiple reaction chambers the flow rates and yields can be more precisely tailored for a variety of situations that may call for particular flow rates and yields. Additionally, the use of the dry chemicals would allow for a long self-life allowing the apparatus to be particularly useful in emergency situations.
Abstract:
Reactors including a chamber having a mixing apparatus within the chamber are provided. Reactors are also provided that include a chamber with a separation apparatus and/or a catalyst apparatus within the chamber. Reactor assemblies are provided that can include: a base configured to define at least a portion of a reaction chamber volume, a separation apparatus within the reaction chamber volume, a catalyst apparatus within the reaction chamber volume, and a lid coupled to both the separation and catalyst apparatuses. Production processes are provided that can include combining at least two reactants within a chamber to form a gas-phase reaction mixture and mechanically mixing the mixture within the chamber to form a product.
Abstract:
A hydrogen iodide manufacturing method which includes a step of producing aqueous solution of hydrogen iodide and sulfuric acid by causing iodine-containing aqueous solution and sulfur dioxide to react with each other in a pressurized condition. The pressurized condition may be of not lower than 0.1 MPa in gauge pressure. The method may further include: a separation step of adding iodine to the aqueous solution of hydrogen iodide and separating an upper phase containing sulfuric acid relatively to a large extent and a lower phase containing hydrogen iodide relatively to a large extent; and a step of producing hydrogen iodide by adding sulfur dioxide to the upper phase in a pressurized condition and extracting the produced hydrogen iodide to the lower phase.
Abstract:
An apparatus is provided to generate a gas by mixing chemicals with water. Typically, the production of gas, particularly oxygen, by combining water with powders and other dry chemicals has not been widely employed. There have existed a number of preexisting barriers such as undesirable flow rates and yields. However, by utilizing multiple reaction chambers the flow rates and yields can be more precisely tailored for a variety of situations that may call for particular flow rates and yields. Additionally, the use of the dry chemicals would allow for a long self-life allowing the apparatus to be particularly useful in emergency situations.
Abstract:
An apparatus is provided to generate a gas by mixing chemicals with water. Typically, the production of gas, particularly oxygen, by combining water with powders and other dry chemicals has not been widely employed. There have existed a number of preexisting barriers such as undesirable flow rates and yields. However, by utilizing multiple reaction chambers the flow rates and yields can be more precisely tailored for a variety of situations that may call for particular flow rates and yields. Additionally, the use of the dry chemicals would allow for a long self-life allowing the apparatus to be particularly useful in emergency situations.
Abstract:
Devices and processes for the simultaneous transfer of liquids from a source container to a target container are disclosed. The source container includes a multitude of source sub-containers, and the target container includes a multitude of target sub-containers. The device includes a multitude of tubes arranged in a matrix, each tube having an entrance and exit.
Abstract:
Two methods and apparatuses are described for hydrazine synthesis through nitrogen fixation induced by photoexcitation of N2. Both methods of photoexcitation of N2 for hydrazine synthesis involve a two-photon absorption process. The first method of N2 fixation with H2 uses a high-energy short-pulsed Nd: YAG laser with wavelength of 1.06 μm. The two-photon absorption of N2 is followed by a vibrational-vibrational (V—V) energy transfer that leads to a near-complete population inversion of N2 vibrational states. The energy separation of these states is larger than the activation energy needed for N2H4 formation. The second method of N2 fixation with H2O uses a high-energy short-pulsed blue laser with wavelength of 0.4 μm. The two-photon absorption at 0.4 μm pumps N2 to a highly excited vibrational state, which has enough energy to both dissociate H2O into H2 and O2, and to react with H2 to form N2H4 as in the above direct method of N2 fixation with H2.
Abstract translation:描述了通过N 2光激发引起的氮固定的肼合成的两种方法和装置。 用于肼合成的N 2的光激发的两种方法涉及双光子吸收过程。 使用H 2 N 2固定的第一种方法使用波长为1.06μm的高能短脉冲Nd:YAG激光器。 N 2的双光子吸收之后是振动振动(V-V)能量转移,其导致N 2个振动状态的接近完全的群体反转。 这些状态的能量分离大于N 2 H 4 H 4形成所需的活化能。 使用H 2 O 2固定的第二种N 2方法使用波长为0.4μm的高能短脉冲蓝色激光。 将0.4毫升泵N 2的双光子吸收到高激发的振动状态,其具有足够的能量以将H 2 O解离成H 2 O 2, 并与H 2 H 2反应形成N 2 H 4 H 4,如上所述 用H 2 N直接固定N 2固定。