Process for conversion of hydrocarbon feed to c2 unsaturated hydrocarbons and syngas composition used for multiple applications
US-2019233350-A1 · Aug 1, 2019 · US
US11939451B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11939451-B2 |
| Application number | US-202117177636-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 17, 2021 |
| Priority date | Feb 20, 2020 |
| Publication date | Mar 26, 2024 |
| Grant date | Mar 26, 2024 |
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A composition comprising acetylene fluid at least partially solubilized in an improved solvent is described. The improved solvents exhibit non-toxicity and are further characterized by low vapor pressures to minimize solvent carryover during delivery of the acetylene fluid, while retaining suitable acetylene solubilizing capacity.
Opening claim text (preview).
The invention claimed is: 1. An acetylene fluid supply package, comprising: a pressure vessel; a porous filler in the pressure vessel; an improved solvent within the porous filler, said solvent solubilizing with acetylene absorbed within the improved solvent; said improved solvent comprising all of the following attributes: (i) a vapor pressure at 20 deg of approximately 6 torr or less; (ii) a Hansen solubility factor (dH) greater than about 5 MPa0.5; (iii) higher non-toxicity in comparison to dimethylformamide (DMF) and N-methylpyrrolidone (NMP); and (iv) a chemical structure comprising O, N or F atoms, wherein at least one of said O, N or F atoms is not bonded to a hydrogen atom, and further wherein said chemical structure is characterized by an absence of phosphorus boron, calcium and nickel; wherein the improved solvent is mesityl oxide, said mesityl oxide loaded into the pressure vessel in an amount no greater than about 0.54 kg of mesityl oxide per liter of volume of the pressure vessel. 2. The acetylene fluid supply package of claim 1 , wherein the improved solvent is mesityl oxide, said mesityl oxide loaded into the pressure vessel in an amount no greater than about 0.51 kg of mesityl oxide per liter of volume the pressure vessel. 3. The acetylene fluid supply package of claim 1 , wherein the improved solvent is mesityl oxide loaded into the pressure vessel in an amount no greater than about 0.49 kg of mesityl oxide per liter of volume of the pressure vessel. 4. A system comprising at least one acetylene fluid supply package and an acetylene-utilizing process tool in fluid communication with the at least one acetylene fluid supply package, said at least one acetylene fluid supply package comprising a pressure vessel; a porous filler in the pressure vessel; an improved solvent within the porous filler, said improved solvent solubilizing with acetylene absorbed within the improved solvent; said improved solvent comprising all of the following attributes: (i) a vapor pressure at 20 deg of approximately 9 torr or less; (ii) a Hansen solubility factor (dH) greater than about 5 MPa0.5; (iii) higher non-toxicity in comparison to dimethylformamide (DMF) and N-methylpyrrolidone (NMP); and (iv) a chemical structure comprising O, N or F atoms, wherein at least one of said O, N or F atoms is not bonded to a hydrogen atom, and further wherein said chemical structure is characterized by an absence of phosphorus, boron, calcium and nickel; wherein the at least one acetylene fluid supply package is configured to allow a discharge of the acetylene fluid under dispensing conditions; and further wherein said acetylene-utilizing process tool is configured to receive the acetylene fluid from the at least one acetylene fluid supply package. 5. An acetylene fluid supply package, comprising: a pressure vessel; a porous filler in the pressure vessel; an improved solvent within the porous filler, said solvent solubilizing with acetylene absorbed within the improved solvent; said improved solvent comprising all of the following attributes: (i) a vapor pressure at 20 deg of approximately 6 torr or less; (ii) a Hansen solubility factor (dH) greater than about 5 MPa0.5; (iii) higher non-toxicity in comparison to dimethylformamide (DMF) and N-methylpyrrolidone (NMP); and (iv) a chemical structure comprising O, N or F atoms, wherein at least one of said O, N or F atoms is not bonded to a hydrogen atom, and further wherein said chemical structure is characterized by an absence of phosphorus boron, calcium and nickel; wherein the improved solvent is pentoxone, said pentoxone loaded into the pressure vessel in an amount no greater than about 0.55 kg of pentoxone per liter of volume of the pressure vessel. 6. The acetylene fluid supply package of claim 5 , wherein the improved solvent is pentoxone, said pentoxone loaded into the pressure vessel in an amount no greater than about 0.53 kg of pentoxone per liter of volume of the pressure vessel. 7. The acetylene fluid supply package of claim 5 , wherein the improved solvent is pentoxone, said pentoxone loaded into the pressure vessel in an amount no greater than about 0.50 kg of pentoxone per liter of volume of the pressure vessel. 8. A system comprising at least one acetylene fluid supply package and an acetylene-utilizing process tool in fluid communication with the at least one acetylene fluid supply package, said at least one acetylene fluid supply package comprising a pressure vessel; a porous filler in the pressure vessel; an improved solvent within the porous filler, said improved solvent solubilizing with acetylene absorbed within the improved solvent; said improved solvent comprising all of the following attributes: (i) a vapor pressure at 20 deg of approximately 6 torr or less; (ii) a Hansen solubility factor (dH) greater than about 5 MPa0.5; (iii) higher non-toxicity in comparison to dimethylformamide (DMF) and N-methylpyrrolidone (NMP); and (iv) a chemical structure comprising 0, N or F atoms, wherein at least one of said 0, N or F atoms is not bonded to a hydrogen atom, and further wherein said chemical structure is characterized by an absence of phosphorus, boron, calcium and nickel; wherein the at least one acetylene fluid supply package is configured to allow a discharge of the acetylene fluid under dispensing conditions; and further wherein said acetylene-utilizing process tool is configured to receive the acetylene fluid from the at least one acetylene fluid supply package; and further wherein the improved solvent is either mesityl oxide, said mesityl oxide loaded into the pressure vessel in an amount no greater than about 0.54 kg of mesityl oxide per liter of volume of the pressure vessel, or pentoxone, said pentoxone loaded into the pressure vessel in an amount no greater than about 0.55 kg of pentoxone per liter of volume of the pressure vessel.
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