Solvent free oil soluble drag reducing polymer suspension

Claim 3

A method as described in claim 1 wherein the bulk polymerization reaction is carried out in a reactor of no more than nine inches in its smallest dimension.

Claim 4

A method as described in claim 2 wherein the catalyst used is a Ziegler/Natta olefin polymerization catalyst.

Claim 5

A method as described in claim 3 wherein the catalyst and reactants are contacted at a temperature of from 0° C. to about 40° C.

Claim 6

A process for producing a finely divided, non-crystalline, ultra-high molecular weight hydrocarbon-soluble drag-reducing polyolefin which is useful to improve flow of hydrocarbons in conduits which comprises: (a) combining at least one 1-olefin containing from 2 to 40 carbon atoms with a polymerization catalyst in a crystalline, hydrocarbon-insoluble organic reaction enclosure capable of substantially preventing passage of oxygen and water, the enclosure being of such size and shape as to effect high heat conductivity from said crystalline, hydrocarbon insoluble, organic polymer reaction enclosure to the exterior environment, (b) carrying out bulk polymerization of the olefin while removing sufficient heat from the polymerization reaction within the crystalline, hydrocarbon-insoluble reaction enclosure to maintain the polymerization reaction at a temperature suitable for production of non-crystalline, ultra-high molecular weight hydrocarbon-soluble polyolefin for a time sufficient to obtain such polymer, at a conversion level of at least 80% by weight based on total reactor content weight, (c) reducing both the crystalline, hydrocarbon-insoluble organic reaction enclosure and contained bulk polymerized, non-crystalline, ultra-high molecular weight hydrocarbon soluble polyolefin polymer to a finely divided state at a cryogenic temperature below the glass transition temperature of said non-crystalline, ultra-high molecular weight polyolefin drag reducing polymer.

Claim 7

A process for producing a finely divided, non-crystalline, ultra-high molecular weight hydrocarbon-soluble drag-reducing polyolefin which is useful to improve flow of hydrocarbons in conduits which comprises: (a) combining at least one 1-olefin containing from 2 to 40 carbon atoms with a polymerization catalyst in a crystalline, hydrocarbon-insoluble organic reaction enclosure capable of substantially preventing passage of oxygen and water, the enclosure being of such size and shape as to effect high heat conductivity from said crystalline, hydrocarbon insoluble, organic polymer reaction enclosure to the exterior environment, (b) carrying out bulk polymerization of the olefin while removing sufficient heat from the polymerization reaction within the crystalline, hydrocarbon-insoluble reaction enclosure to maintain the polymerization reaction at a temperature suitable for production of non-crystalline, ultra-high molecular weight hydrocarbon-soluble polyolefin for a time sufficient to obtain such polymer, at a conversion level of at least 80% by weight based on total reactor content weight, (c) reducing both the crystalline, hydrocarbon-insoluble organic reaction enclosure and contained bulk polymerized, non-crystalline, ultra-high molecular weight hydrocarbon soluble polyolefin polymer to a finely divided state at a cryogenic temperature below the glass transition temperature of said non-crystalline, ultra-high molecular weight polyolefin drag reducing polymer.

Claim 8

The process of claim 5 wherein the finely divided product of (c) is combined with a water soluble polymeric thickening agent and a suspending material selected from the group consisting of water and water-alcohol mixtures under agitation conditions to obtain stable, non-agglomerating suspensions.

Claim 9

The process of claim 5 wherein the polymerization catalyst is a Ziegler-Natta polymerization catalyst, and wherein the organic polymer forming the reaction enclosure is multi-layered, comprising a crystalline polyolefin on either side of an oxygen barrier polymer, wherein the reaction is carried out in the absence of any solvent other than the reactants, and wherein the reaction mixture temperature is maintained in the range of about -10° F. to about 150° F.

Claim 10

The process of claim 7 wherein the reaction enclosure comprises a multi-layered water and oxygen impermeable organic polymer.

Claim 11

The process of claim 8 wherein the reaction vessel outer layers are at least one polyolefin selected from the group consisting of polyethylene, polybutene, and polypropylene, and the oxygen barrier polymer is selected from the group consisting of polyethylene vinyl alcohol copolymer, nylons, polyesters, and polyvinylidene chloride.

Claim 12

The process of claim 9 wherein a coating agent selected from the group consisting of alumina, silica, carbon black, calcined clays, talc, and metal stearates is present on the finely divided polymeric powder.

Claim 13

The process of claim 10 wherein a surfactant is added at levels up to about 3 percent by weight based on total suspension weight.

Claim 14

The process of claim 11 wherein the surfactant is selected from the group consisting of non-ionic surfactants and anionic surfactants.