Abstract: A box style steam methane reformer (15) has plural sections (37), with each section having walls (27-29-31, 33) forming an interior cavity (35) and open ends (43) that communicate with the interior cavity. Each section has a feedstock supply pipe (71) and a fuel supply pipe (63) located along the top wall, as well as a syngas collection pipe (79) and a flue gas collection duct (75) located outside of the bottom wall. The pipes and ducts have ends that are aligned with each other to allow the sections to be assembled together. Burners (67) are in the interior cavity and are connected to the fuel supply pipe. Reactor tubes (59) extend through the interior cavity. Refractory members (81) are located in the interior cavity and across a slot. The spacing between the refractory members varies to control the flow of flue gas.

Abstract: A box style steam methane reformer (15) has plural sections (37), with each section having walls (27-29-31, 33) forming an interior cavity (35) and open ends (43) that communicate with the interior cavity. Each section has a feedstock supply pipe (71) and a fuel supply pipe (63) located along the top wall, as well as a syngas collection pipe (79) and a flue gas collection duct (75) located outside of the bottom wall. The pipes and ducts have ends that are aligned with each other to allow the sections to be assembled together. Burners (67) are in the interior cavity and are connected to the fuel supply pipe. Reactor tubes (59) extend through the interior cavity. Refractory members (81) are located in the interior cavity and across a slot. The spacing between the refractory members varies to control the flow of flue gas.

Abstract: A dry reforming methane to synthesis gas catalyst is provided. The catalyst has a primary metal of magnesia (MgO). A secondary metal is mixed with the primary metal. The primary metal and the secondary metal have crystalline structures that are close to one another so as to be in solid solution with the support and form a mono-crystalline structure.

Abstract: A box style steam methane reformer has plural sections, with each section having walls forming an interior cavity and open ends that communicate with the interior cavity. Each section has a feedstock supply pipe and a fuel supply pipe located along the top wall, as well as a syngas collection pipe and a flue gas collection duct located outside of the bottom wall. The pipes and ducts have ends that are aligned with each other to allow the sections to be assembled together. Burners are located in the interior cavity and are connected to the fuel supply pipe. Reactor tubes extend through the interior cavity. The bottom ends are supported by the syngas collection pipe and the top ends are spring supported to allow for expansion and contraction. Refractory members are located in the interior cavity and across a slot leading to the flue gas collection dust. The spacing between the refractory members varies to control the flow of flue gas.

Abstract: A refrigerator contains a battery pack for providing a DC current to drive a refrigeration system and alternatively is connectable to an AC power source for driving the refrigeration system from the AC power source. The DC battery pack is utilized during peak loads on the AC source of power, and the AC source of power is utilized during reduced loads on the AC power source. The electrical circuitry and components of the AC and DC power circuits are contained within a mechanical compartment located within the refrigerator.

Abstract: A refrigerator contains a battery pack for providing a DC current to drive a refrigeration system and alternatively is connectable to an AC power source for driving the refrigeration system from the AC power source. The DC battery pack is utilized during peak loads on the AC source of power, and the AC source of power is utilized during reduced loads on the AC power source. The electrical circuitry and components of the AC and DC power circuits are contained within a mechanical compartment located within the refrigerator.

Abstract: A DI water purification system for the point-of-use purification of water in applications demanding the highest quality of water. The system includes the following components: 1. dual submicron filters of 0.2 micron rating in parallel, housed in chemically inert housings; 2. a stacked-membrane or spiral-wound Ultrafilter module of nominal rating of 5000 to 100,000 molecular weight; 3. purge flowmeters appropriate to the purge requirements of the Ultrafilter; 4. chemically inert piping, gasket and sealing materials used to join the various sections of the system; and, 5. chemically resistant supports and housings to mechanically fasten the various components together. The DI water purification system is suitable for use in industries such as semiconductor, medical, pharmaceutical, chemical or any other application or use requiring ultrafiltered DI water.

Abstract: Inert liquid gas such as liquid nitrogen or liquid argon is used in vertical melting furnaces to prevent oxidation of the metal during holding periods. The method can be applied to any kind of metal. The use of inert liquid gas for the "blow-dow" of the furnace will flush art all existing furnace atmosphere and prevent oxidation. The casting recovery time may be reduced from about one hour to 15 minutes. Also the layers of oxide resulting from oxidation can be negated, allowing for fewer rejects, if any, during further surface treatment.