초록 ▼

A method of blending delayed coker feedstocks to produce a coke that is easier to remove from a coker drum. A first feedstock is selected having less than about 250 wppm dispersed metals content and greater than about 5.24 API gravity. A second delayed coker feedstock is blended with said first resi

A method of blending delayed coker feedstocks to produce a coke that is easier to remove from a coker drum. A first feedstock is selected having less than about 250 wppm dispersed metals content and greater than about 5.24 API gravity. A second delayed coker feedstock is blended with said first resid feedstock so that the total dispersed metals content of the blend will be greater than about 250 wppm and the API gravity will be less than about 5.24.

대표청구항 ▼

The invention claimed is: 1. A method of increasing the capacity of a delayed coking unit using a delayed coker feedstock having less than 250 wppm dispersed metals content and greater than 5.24 API gravity, the method being to shorten the cycle time of the unit by the steps comprising: selecting o

The invention claimed is: 1. A method of increasing the capacity of a delayed coking unit using a delayed coker feedstock having less than 250 wppm dispersed metals content and greater than 5.24 API gravity, the method being to shorten the cycle time of the unit by the steps comprising: selecting one or more first delayed coker feedstocks, each having less than about 250 wppm dispersed metals content and greater than about 5.24 API gravity; selecting one or more second delayed coker feedstocks and blending said one or more second delayed coker feedstocks into said one or more first delayed coker feedstocks so that the total dispersed metals content of the blended feedstocks will be greater than about 250 wppm and the API gravity will be less than about 5.24; heating said blend of feedstocks to a temperature from about 70�� C. to about 500�� C.; conducting said heated blend of feedstocks to a coker furnace wherein the blend of feedstocks is heated to delayed coking temperatures; conducting said heated blend of feedstocks to a coker drum wherein vapor products are collected overhead and a free-flowing solid shot coke product is produced, quenching the coke with water and draining the free-flowing shot coke product with interstitial water from the coker drum by unheading the drum and permitting the shot coke product to pour out of the drum. 2. The process of claim 1 wherein the one or more first and second feedstocks are selected from the group consisting of vacuum resids and deasphalter bottoms. 3. The process of claim 1 wherein an additive is incorporated in said blend of feedstocks which additive is an organic soluble, organic insoluble, or non-organic miscible metals-containing additive that is effective for the formation of substantially free-flowing coke. 4. The process of claim 3 wherein the additive is added to either said one or more first delayed coker feedstocks or to said one or more second delayed coker feedstocks. 5. The process of claim 3 wherein the additive is added to the blend of said one or more first delayed coker feedstocks and said one or more second delayed coker feedstocks. 6. The process of claim 3 wherein the metal of the additive is selected from the group consisting of sodium, potassium, iron, nickel, vanadium, tin, molybdenum, manganese, aluminum cobalt, calcium, magnesium, and mixtures thereof.