Patent classifications
C01B3/02
Method and system for pelletizing spent bleaching earth
The present disclosure includes a process for pelletizing a spent bleaching earth (SBE) into a clay-biocarbon composite including classifying the SBE based on at least one parameter of the SBE, selecting at least one filler compound and mixing the at least one filler compound with the SBE to make a mixture, forming a plurality of pellets out of the mixture, and pyrolyzing the pellets to produce the clay-biocarbon composite. Pyrolyzing a pelleted spent bleaching earth (SBE) may include advancing the pelleted SBE with a distributer to a first thermal chamber for providing even thermal processing, releasing the pelleted SBE to an auger to cool to room temperature, and condensing at least one volatile compound emitted from the pelleted SBE during thermal processing to produce a condensate for reuse.
Method and system for pelletizing spent bleaching earth
The present disclosure includes a process for pelletizing a spent bleaching earth (SBE) into a clay-biocarbon composite including classifying the SBE based on at least one parameter of the SBE, selecting at least one filler compound and mixing the at least one filler compound with the SBE to make a mixture, forming a plurality of pellets out of the mixture, and pyrolyzing the pellets to produce the clay-biocarbon composite. Pyrolyzing a pelleted spent bleaching earth (SBE) may include advancing the pelleted SBE with a distributer to a first thermal chamber for providing even thermal processing, releasing the pelleted SBE to an auger to cool to room temperature, and condensing at least one volatile compound emitted from the pelleted SBE during thermal processing to produce a condensate for reuse.
GAS PRODUCTION FROM SOLIDS VIA NON-THERMAL PLASMA
A first voltage source produces a first voltage such as an AC voltage. Further, a first electrode of a hydrogen generation system conveys the first voltage. The first voltage conveyed over the first electrode generates low-temperature plasma extending between the first electrode and the mass of material. Presence of the low-temperature plasma releases gas from the mass of material.
GAS PRODUCTION FROM SOLIDS VIA NON-THERMAL PLASMA
A first voltage source produces a first voltage such as an AC voltage. Further, a first electrode of a hydrogen generation system conveys the first voltage. The first voltage conveyed over the first electrode generates low-temperature plasma extending between the first electrode and the mass of material. Presence of the low-temperature plasma releases gas from the mass of material.
System and Method for Enhanced Petroleum Product Recovery
A system for producing CO and CO.sub.2 to achieve an efficient oil recovery operation having de minimis undesirable gaseous emissions is provided. The system includes a portable CO producing device and a portable CO.sub.2 producing device located proximate to the reservoir and a gas collecting device configured to receive CO and CO.sub.2 and selectively distribute a desired ratio of CO and CO.sub.2 dynamically based on current reservoir conditions. Producing CO.sub.2 proximate to the reservoir comprises reforming carbon based fuel within oxygen. Electrical energy generated is used to selectively distribute the desired ratio of CO/CO.sub.2 to the reservoir with de minimis greenhouse gases produced transmitted into the atmosphere. The system is an energy efficient arrangement that recycles and reuses by-products and unused products from the process. Greenhouse gas emissions are significantly reduced compared to conventional processes by-products are fully utilized. Hydrogen produced can be used to generate electricity, as can heat generated from other sources within the process.
System and Method for Enhanced Petroleum Product Recovery
A system for producing CO and CO.sub.2 to achieve an efficient oil recovery operation having de minimis undesirable gaseous emissions is provided. The system includes a portable CO producing device and a portable CO.sub.2 producing device located proximate to the reservoir and a gas collecting device configured to receive CO and CO.sub.2 and selectively distribute a desired ratio of CO and CO.sub.2 dynamically based on current reservoir conditions. Producing CO.sub.2 proximate to the reservoir comprises reforming carbon based fuel within oxygen. Electrical energy generated is used to selectively distribute the desired ratio of CO/CO.sub.2 to the reservoir with de minimis greenhouse gases produced transmitted into the atmosphere. The system is an energy efficient arrangement that recycles and reuses by-products and unused products from the process. Greenhouse gas emissions are significantly reduced compared to conventional processes by-products are fully utilized. Hydrogen produced can be used to generate electricity, as can heat generated from other sources within the process.
PROCESS AND PLANT FOR THE PURIFICATION OF RAW SYNTHESIS GAS
A process for the stepwise separation of accompanying gases from a raw synthesis gas stream by a liquid absorbent countercurrently guided through all process steps and circulated via regeneration plants, wherein either the accompanying gases H.sub.2S, COS and CO.sub.2 are separated in a common absorption step or, in one of the selective absorption steps chiefly H.sub.2S and COS are separated and in the next step in flow direction of the gas chiefly CO.sub.2 is separated, and in the last step a separation of accompanying gas residues (fine wash) is effected, wherein before the separation of H.sub.2S and COS an absorption step chiefly for the separation of aromatics and subsequently an absorption step chiefly for the separation of methyl mercaptan is carried out.
PROCESS AND PLANT FOR THE PURIFICATION OF RAW SYNTHESIS GAS
A process for the stepwise separation of accompanying gases from a raw synthesis gas stream by a liquid absorbent countercurrently guided through all process steps and circulated via regeneration plants, wherein either the accompanying gases H.sub.2S, COS and CO.sub.2 are separated in a common absorption step or, in one of the selective absorption steps chiefly H.sub.2S and COS are separated and in the next step in flow direction of the gas chiefly CO.sub.2 is separated, and in the last step a separation of accompanying gas residues (fine wash) is effected, wherein before the separation of H.sub.2S and COS an absorption step chiefly for the separation of aromatics and subsequently an absorption step chiefly for the separation of methyl mercaptan is carried out.
Hydrogen gas generator
A hydrogen generator, a fuel pellet assembly for use in the hydrogen generator and a fuel cell system are disclosed. The hydrogen generator includes a housing having a lid pivotally connected to a base and a strip having a plurality of heaters on one side and a second plurality of heaters on the opposite side. A first cartridge is disposed on one side of the strip and a second cartridge is disposed on the opposite side. Each of the first and second cartridges has a plurality of fuel pellets, each including a hydrogen-containing material that will release hydrogen gas when heated. The heaters are selectively activated to heat one or more fuel pellets to initiate the release of hydrogen gas.
Hydrogen gas generator
A hydrogen generator, a fuel pellet assembly for use in the hydrogen generator and a fuel cell system are disclosed. The hydrogen generator includes a housing having a lid pivotally connected to a base and a strip having a plurality of heaters on one side and a second plurality of heaters on the opposite side. A first cartridge is disposed on one side of the strip and a second cartridge is disposed on the opposite side. Each of the first and second cartridges has a plurality of fuel pellets, each including a hydrogen-containing material that will release hydrogen gas when heated. The heaters are selectively activated to heat one or more fuel pellets to initiate the release of hydrogen gas.