IP Library Granted Patent US 12703833
Granted Patent B2
US 12703833 · App. 18/820,022 · Granted Aug 11, 2026

Alkylated napthalene blendstocks and processes for producing the same

Inventors: Jorg F. W. Weber (Houston, TX); Michael L. Blumenfeld (Annandale, NJ); Harrison T. Hawkins (Medford, NJ); William W. Lonergan (Humble, TX); Zachary D. Young (Lansdale, PA); Sina Sartipi (Willebroek, BE); Mabel G. Lam (Seabrook, TX); Samuel J. Caterina (League City, TX)
Assignee: ExxonMobil Technology and Engineering Company
C10M105/06B01J29/7038C10M177/00C10M2203/1065C10N2020/02C10N2020/06C10N2020/067C10N2070/00
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Quick Facts
Patent No.
US 12703833
App. No.
18/820,022
Granted
Aug 11, 2026
Kind
B2
Abstract

Alkylated naphthalene blendstock and processes for making the alkylated naphthalene blendstock are provided. The present processes comprise mixing an acid-form MWW-type catalyst, naphthalene, and a solvent to provide a reaction mixture and adding linear alpha olefins to the reaction mixture after heating. The resulting AN blendstock has an isomer ratio of less than 45 wt % mono alkylated naphthalene and greater than 55 wt % multi-alkylated naphthalene and can be combined with polyalphaolefin base stock to provide a synthetic lubricant formulation produced without triflic catalyst and with less process steps.

Claims (14)

1 . A process for making an alkylated naphthalene (AN) blendstock comprising the steps of:

mixing an acid-form MWW-type catalyst, naphthalene, and a solvent to provide a reaction mixture, wherein the acid-form MWW-type catalyst has an average particle distribution between 55 μm and 85 μm, a surface area between 475 and 600 m 2 /g, and a total acidity of between 0.80 and 1.0 meq/g TPAD;

increasing the temperature of the reaction mixture; and

adding linear alpha olefins to the reaction mixture to produce the AN blendstock comprising an isomer ratio of less than 45 wt % mono alkylated naphthalene and greater than 55 wt % multi-alkylated naphthalene, wherein the linear alpha olefins comprise LAO14 or LAO16.

2 . The process for making an AN blendstock of claim 1 , wherein the AN blendstock has a kinematic viscosity between about 7.0 and 9.5 cSt KV100 as measured by D445.

3 . The process for making an AN blendstock of claim 1 , wherein the acid-form MWW-type catalyst is MCM-22H.

4 . The process for making an AN blendstock of claim 1 , wherein the catalyst load is less than 1.5 wt %.

5 . The process for making an AN blendstock of claim 1 , wherein the multi-alkylated naphthalene comprises di-alkylated naphthalene and tri-alkylated naphthalene.

6 . The process for making an AN blendstock of claim 1 , wherein the AN blendstock comprises more than 30 wt % di-alkylated naphthalene.

7 . The process for making an AN blendstock of claim 1 , wherein at least 98 wt % of naphthalene is converted.

8 . The process for making an AN blendstock of claim 1 , where the AN blendstock is made without triflic catalyst.

9 . The process for making an AN blendstock of claim 1 , wherein the linear alpha olefins are a mPAO.

10 . The process for making an AN blendstock of claim 1 , wherein the linear alpha olefins are a hybrid PAO.

11 . The process for making an AN blendstock of claim 1 , wherein the linear alpha olefins comprise at least two different linear alpha-olefins selected from C 3 to C 30 LAO.