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A process is described for introducing a catalyst into a polymerization zone by detecting one or a combination of (i) a change in a concentration of the catalyst in a catalyst feed stream upstream of the polymerization zone, (ii) a change in a concentration of monomer in the polymerization zone, and

A process is described for introducing a catalyst into a polymerization zone by detecting one or a combination of (i) a change in a concentration of the catalyst in a catalyst feed stream upstream of the polymerization zone, (ii) a change in a concentration of monomer in the polymerization zone, and (iii) a change in a polymer production rate of the polymerization zone, adjusting a first catalyst flow rate of the catalyst in the catalyst feed stream to a second catalyst flow rate based on the one or a combination of (i), (ii), and (iii), and introducing the catalyst into the polymerization zone downstream of a location in the catalyst feed stream where the step of adjusting is performed. A catalyst injection system for carrying out such a process is also provided.

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1. A process for introducing a catalyst into a polymerization zone, the process comprising: detecting one or a combination selected from a group consisting of:i) a change in a concentration of the catalyst in a catalyst feed stream upstream of the polymerization zone,ii) a change in a concentration

1. A process for introducing a catalyst into a polymerization zone, the process comprising: detecting one or a combination selected from a group consisting of:i) a change in a concentration of the catalyst in a catalyst feed stream upstream of the polymerization zone,ii) a change in a concentration of monomer in the polymerization zone, andiii) a change in a polymer production rate of the polymerization zone;adjusting a first catalyst flow rate of the catalyst in the catalyst feed stream to a second catalyst flow rate based on the one or a combination selected from a group consisting of i), ii), and iii); andintroducing the catalyst into the polymerization zone downstream of a location in the catalyst feed stream where the step of adjusting is performed;wherein each of the first catalyst flow rate and the second catalyst flow rate is a value of about 0.3 lb/h (0.14 kg/h) to about 0.120 lb/h (54.4 kg/h). 2. The process of claim 1, wherein the polymerization zone comprises one or more of a batch reactor, a continuous stirred tank reactor, a loop slurry reactor, a gas phase reactor, an autoclave reactor, and a tubular reactor having a configuration of one or more of a fluidized bed, a fixed bed, a stirred bed, and a stirred fluidized bed. 3. The process of claim 1, further comprising: downstream of the location in the catalyst feed stream where the step of adjusting is performed, combining the catalyst with a diluent to yield a catalyst system stream; andintroducing the catalyst system stream to the polymerization zone. 4. The process of claim 3, further comprising: prior to the step of introducing the catalyst system stream to the polymerization zone, introducing contents comprising the catalyst and the diluent to a precontactor having at least two mixing stages arranged in series, each of the at least two mixing stages being in a continuous-stirred-tank-reactor configuration,wherein greater than about 70% of the contents pass through the precontactor in one residence time,wherein one residence time in the range of from about 5 minutes to about 30 minutes, andwherein the catalyst flows into the polymerization zone via an effluent of the precontactor. 5. The process of claim 4, wherein the catalyst is a chromium-based catalyst. 6. The process of claim 4, wherein a first portion of the effluent is recirculated to a first stage of the at least two mixing stages, and wherein a second portion of the effluent flows to the polymerization zone. 7. The process of claim 1, wherein the catalyst is a Ziegler-Natta catalyst or a metallocene catalyst, the process further comprising: detecting a change in concentration of a co-catalyst in a co-catalyst feed stream upstream of the polymerization zone;adjusting a first co-catalyst flow rate in the co-catalyst feed stream to a second co-catalyst flow rate based on the change in concentration of the co-catalyst;introducing the co-catalyst into the polymerization zone downstream of a location in the co-catalyst feed stream where the step of adjusting the first co-catalyst flow rate is performed. 8. The process of claim 7, wherein the catalyst feed stream, the co-catalyst feed stream, and a diluent combine to form a catalyst system stream, which flows into the polymerization zone. 9. The process of claim 7, wherein the catalyst feed stream, the co-catalyst feed stream, and a diluent combine to form a catalyst system stream, the process further comprising: introducing contents comprising the catalyst system stream and a diluent to a precontactor having at least two mixing stages in series, each of the at least two mixing stages being in a continuous-stirred-tank-reactor configuration,wherein greater than about 70% of the contents pass through the precontactor in one residence time of, or greater than, about 5 minutes to about 30 minutes, andwherein the catalyst and the co-catalyst flow into the polymerization zone via an effluent of the precontactor. 10. The process of claim 9, wherein a first portion of the effluent is recirculated to a first stage of the at least two mixing stages, and wherein a second portion of the effluent flows to the polymerization zone. 11. The process of claim 7, wherein the catalyst is a metallocene catalyst, the process further comprising: detecting a change in concentration of an activator in a activator feed stream upstream of the polymerization zone;adjusting a first activator flow rate in the activator feed stream to a second activator flow rate based on the change in concentration of the activator; andintroducing the activator into the polymerization zone downstream of a location in the activator feed stream where the step of adjusting the first activator flow rate is performed. 12. The process of claim 11, wherein the catalyst feed stream, the co-catalyst feed stream, the activator feed stream, and a diluent combine to form a catalyst system stream which flows into the polymerization zone. 13. The process of claim 11, wherein the catalyst feed stream, the co-catalyst feed stream, the activator feed stream, and a diluent combine to form a catalyst system stream, the process further comprising: introducing contents comprising the catalyst system stream and a diluent to a precontactor having at least two mixing stages in series, each of the at least two mixing stages being in a continuous-stirred-tank-reactor configuration,wherein greater than about 70% of the contents pass through the precontactor in one residence time of, or greater than, about 5 minutes to about 30 minutes, andwherein the catalyst, the co-catalyst, and the activator flow into the polymerization zone via an effluent of the precontactor. 14. The process of claim 13, wherein a first portion of the effluent is recirculated to a first stage of the at least two mixing stages, and wherein a second portion of the effluent flows to the polymerization zone. 15. A catalyst injection system comprising: a catalyst stream;a diluent stream; anda precontactor comprising at least two mixing stages arranged in series, each of the at least two mixing stages being in continuous-stirred-tank-reactor configuration,wherein a first stage of the at least two mixing stages receives contents comprising a catalyst obtained from the catalyst stream and a diluent obtained from the diluent stream, andwherein the precontactor is configured such that greater than about 70% of the contents pass through the at least two mixing stages in one residence time of about 5 minutes to about 30 minutes. 16. The catalyst injection system of claim 15, wherein the precontactor further comprises: a recirculation pump positioned to receive an effluent of the precontactor; anda flow controller positioned between the recirculating pump and a polymerization zone, wherein the recirculation pump recycles via a recycle stream a first portion of the effluent to the first stage of the at least two mixing stages and pumps a second portion of the effluent to the flow controller, and wherein the flow controller controls a flow of the second portion to the polymerization zone. 17. The catalyst injection system of claim 15, wherein the precontactor includes the at least two mixing stages contained in a single vessel which are defined by internals of the vessel, wherein one or more agitators in the vessel mix the contents passing through each of the at least two mixing stages. 18. The catalyst injection system of claim 15, wherein the catalyst stream includes a catalyst flow control device which adjusts a first catalyst flow rate to a second catalyst flow rate upon a detection of a change in one or a combination selected from the group consisting of: i) a concentration of the catalyst in the catalyst stream;ii) a concentration of monomer in a polymerization zone; andiii) a polymer production rate of the polymerization zone. 19. The catalyst injection system of claim 18, further comprising: at least one of: a co-catalyst stream, wherein the first stage of the at least two mixing stages receives a co-catalyst obtained from the co-catalyst stream, wherein the co-catalyst stream includes a co-catalyst flow control device which adjusts a first co-catalyst flow rate to a second co-catalyst flow rate upon a detection of a change in a concentration of the co-catalyst in the co-catalyst stream; oran activator stream, wherein the first stage of the at least two mixing stages receives an activator obtained from the activator stream, wherein the activator stream includes an activator flow control device which adjusts a first activator flow rate to a second activator flow rate upon a detection of a change in a concentration of the activator in the activator stream,and wherein the contents which are received by the precontactor further comprise the co-catalyst, the activator, or both. 20. The process of claim 1 wherein the monomer comprises ethylene. 21. The catalyst injection system of claim 16, wherein the recycle stream further comprises a solids analyzer configured to determine the solids content within the recycle stream;wherein the catalyst injection system further comprises a solids make-up system feeding solids to the precontactor; andwherein the solids analyzer sends a signal to a solids flow control device to adjust a flow of solids from the solids make-up system to the precontactor as needed to maintain a desired solids level in the precontactor. 22. The catalyst injection system of claim 21, further comprising a level indicator configured to determine a fluid level within the precontactor and send a signal to a diluent flow control device to adjust a flow of diluent to the precontactor as needed to maintain a desired solids level in the precontactor. 23. The catalyst injection system of claim 22, wherein the solids make-up system further comprises a mudpot or a weigh feeder. 24. The catalyst injection system of claim 19, wherein the catalyst stream comprises a metallocene catalyst, the co-catalyst stream comprises an aluminum alkyl component, the activator stream comprises a super solid acid (SSA) initiator, and the monomer comprises ethylene. 25. The catalyst injection system of claim 17, wherein the recycle stream further comprises a solids analyzer configured to determine the solids content within the recycle stream;wherein the catalyst injection system further comprises a solids make-up system feeding solids to the precontactor;wherein the solids make-up system further comprises a mudpot or a weigh feeder;wherein the solids analyzer sends a signal to a solids flow control device to adjust a flow of solids from the solids make-up system to the precontactor as needed to maintain a desired solids level in the precontactor; andwherein the catalyst injection system further comprises a level indicator configured to determine a fluid level within the precontactor and send a signal to a diluent flow control device to adjust a flow of diluent to the precontactor as needed to maintain a desired solids level in the precontactor.