WO1994003324A1

WO1994003324A1 - Process for making silicone containing hydrogel lenses

Info

Publication number: WO1994003324A1
Application number: PCT/US1993/005827
Authority: WO
Inventors: Rajan Sohansingh Bawa; Yu-Chin Lai; Mahendra Premji Nandu
Original assignee: Bausch & Lomb Incorporated
Priority date: 1992-08-03
Filing date: 1993-06-17
Publication date: 1994-02-17
Also published as: AU4539693A; US5260000A; CA2141571A1; BR9306910A; DE69315581T2; HK1005613A1; MX9304682A; TW285677B; CN1047982C; CA2141571C; CN1085844A; ES2111754T3; DE69315581D1; KR100250192B1; AU669194B2; JP3249123B2; JPH08501504A; EP0652823B1; EP0652823A1

Abstract

A process for preparing silicone hydrogel contact lenses where machining operations are employed to produce a lens having a desired final shape comprises: providing a monomeric mixture comprising a silicone-containing monomer, a hydrophilic monomer and an organic diluent; charging the mixture to a mold and curing the formulation in the mold to obtain a shaped article; removing organic diluent from the shaped article to improve machineability of the article; and machining the shaped article to obtain a contact lens having a desired configuration.

Description

PROCESS FOR MAKING SILICONE CONTAINING

HYDROGEL LENSES

BACKGROUND OF THE INVENTION

The present invention relates to an improved process for making silicone hydrogel lenses.

Hydrogels represent a desirable class of materials for contact lenses. A hydrogel is a hydrated cross-linked polymeric system that contains water in an equilibrium state. Hydrogel lenses offer relatively high oxygen permeability as well as desirable biocompatibility and comfort.

Conventional hydrogel lenses are prepared from monomeric mixtures predominantly containing

hydrophilic monomers such as 2-hydroxyethyl

methacrylate or N-vinyl pyrrolidone. Oxygen

permeability of these conventional hydrogel

materials relates to the water content of the materials. More recently, it has been desired to increase the oxygen permeability of hydrogel lenses by employing silicone-containing monomers in the hydrogel formulations since silicone based materials have higher oxygen permeability than water.

Silicone hydrogels (i.e., hydrogels containing silicone) are usually prepared by polymerizing a mixture containing at least one silicone-containing monomer and at least one hydrophilic monomer.

Either the silicone-containing monomer or the hydrophilic monomer may function as a crosslinking agent (a crosslinker being defined as a monomer having multiple polymerizable functionalities) or a separate crosslinker may be employed. Various processes are known for curing a monomeric mixture in the production of contact lenses, including spincasting and static casting. Spincasting methods are disclosed in U.S. Patent Nos. 3,408,429 and 3,660,545, and static casting methods are disclosed in U.S. Patent Nos. 4,113,224 and 4,197,266. Curing of the monomeric mixture is often followed by a machining operation in order to provide a contact lens having a desired final configuration.

According to several known techniques for manufacturing contact lenses, the casting process may yield a shaped article having the desired posterior and anterior lens surfaces. For example, in static casting processes, a monomeric mixture can be charged to a mold comprising a first mold section including a surface for forming a desired anterior lens surface and a second mold section including a surface for forming a desired posterior lens

surface. In spincasting processes, the monomeric mixture can be charged to an open mold having a surface for forming a desired anterior lens surface, and a desired posterior lens surface is formed from rotation of the mold. However, machining

operations, subsequent to the curing of the article, may still be necessary to provide a contact lens more suitable for placement on the eye. Such machining operations include lathe cutting the lens to obtain a desired edge, buffing the lens edge or polishing the lens edge or surface.

In other known manufacturing techniques, the casting process may yield a shaped article which does not have the desired anterior and/or posterior lens surfaces. Accordingly, the casting process is followed by a machining operation to form a desired lens surface. As an example, U.S. Patent No.

4,555,732 discloses a process where an excess of a monomeric mixture is cured by spincasting in a mold to form a shaped article having an anterior lens surface and a relatively large thickness, and the posterior surface of the cured spincast article is subsequently lathe cut to provide a contact lens having the desired thickness and posterior lens surface. Further machining operations may follow the lathe cutting of the lens surface, such as the previously described edge finishing operations.

However, difficulties have been encountered in attempts to employ such methods which involve machining operations in the production of silicone hydrogel contact lenses. For example, silicone hydrogel articles generally are more difficult to machine than conventional hydrogel articles, as hydrogels prepared from silicone-containing monomers tend to be softer and more rubbery than hydrogels prepared from only the conventional monomers, especially when cast with a diluent.

SUMMARY OF THE INVENTION

The present invention provides a process for preparing silicone hydrogel contact lenses where machining operations are employed to produce a lens having a desired final shape. The process

comprises:

providing a monomeric mixture comprising a silicone-containing monomer, a hydrophilic monomer and an organic diluent;

charging the mixture to a mold and curing the mixture in the mold to obtain a shaped article; removing organic diluent from the shaped article to improve machineability of the article; and

machining the shaped article to obtain a contact lens having a desired configuration.

DETAILED DESCRIPTION OF THE INVENTION

Any known silicone hydrogel formulation including at least one silicone-containing monomer and at least one hydrophilic monomer may be used in the process of this invention, as will be apparent to one skilled in the art. The monomers may be added to the monomeric mixture from which a shaped article is obtained as monomers or prepolymers. Thus, it is understood that the terms "silicone-containing monomers" and "hydrophilic monomers" include prepolymers. Examples of silicone-containing monomers may be found in United States Patent Nos. 4,136,250; 4,153,641; 4,740,533;

5,034,461; and 5,070,215.

Further examples of suitable silicone-containing monomers are bulky polysiloxanylalkyl (meth) acrylic monomers represented by formula (I):

wherein:

X denotes -O- or -NR-; each R independently denotes hydrogen or methyl;

each R¹ independently denotes a lower alkyl radical or a phenyl radical; and

f is 1 or 3 to 10.

Such bulky monomers include methacryloxypropyl tris(trimethylsiloxy) silane, pentamethyldisiloxanyl methylmethacrylate, tris(trimethylsiloxy)

methacryloxy propylsilane, phenyltetramethyldisiloxanylethyl acetate, and

methyldi (trimethylsiloxy)methacryloxymethyl silane.

One preferred class of silicone-containing monomers is a poly(organosiloxane) prepolymer represented by formula (II):

wherein:

each A' independently denotes an activated unsaturated group, such as an ester or amide of an acrylic or a methacrylic acid;

each of R³, R⁴, R⁵ and R⁶ are independently selected from the group consisting of a monovalent hydrocarbon radical or a halogen substituted

monovalent hydrocarbon radical having 1 to 18 carbon atoms which may have ether linkages between carbon atoms;

R⁷ denotes a divalent hydrocarbon radical having from 1 to 22 carbon atoms; and

n is 0 or an integer greater than or equal to 1.

Another preferred class of silicone containing monomers includes silicone-containing vinyl carbonate or vinyl carbamate monomers of formula (III):

wherein:

Y' denotes -O-, -S- or -NH-;

R^Si denotes a silicone-containing organic radical;

R⁸ denotes hydrogen or methyl;

d is 1, 2, 3 or 4; and

q is 0 or 1.

Suitable silicone-containing organic radicals

R^Si include the following:

-(CH₂)_n, Si[(CH₂)_m,CH₃]₃

-(CH₂)_n, Si[OSi(CH₂)_m,CH₃]₃ ; and

wherein:

R¹⁰ denotes wherein p' is 1 to 6;

R¹¹ denotes an alkyl radical or a fluoroalkyl radical having 1 to 6 carbon atoms;

e is 1 to 200;

n' is 1, 2, 3 or 4; and

m' is 0, 1, 2, 3, 4 or 5. The silicone-containing vinyl carbonate or vinyl carbamate monomers specifically include: 1,3- bis[4-vinyloxycarbonyloxy)but-l-yl]tetramethyl- disiloxane; 3-(trimethylsilyl)propyl vinyl

carbonate; 3-(vinyloxycarbonylthio)propyl- [tris(trimethylsiloxy)silane];

3-[tris(trimethylsiloxy)silyl] propyl vinyl

carbamate; 3-[tris(trimethylsiloxy)silyl] propyl allyl carbamate; 3-[tris(trimethylsiloxy)silyl] propyl vinyl carbonate; t-butyldimethylsiloxyethyl vinyl carbonate; trimethylsilylethyl vinyl

carbonate; trimethylsilylmethyl vinyl carbonate; and "V₂D₂₅",

A further preferred class of silicone- containing monomers includes monomers of the

following formulae:

(IV) E(*D*A*D*G)_a*D*A*D*E'; or

(V) E(*D*G*D*A)_a*D*G*D*E'; wherein:

D denotes an alkyl diradical, an alkyl

cycloalkyl diradical, a cycloalkyl diradical, an aryl diradical or an alkylaryl diradical having 6 to 30 carbon atoms;

G denotes an alkyl diradical, a cycloalkyl diradical, an alkyl cycloalkyl diradical, an aryl diradical or an alkylaryl diradical having 1 to 40 carbon atoms and which may contain ether, thio or amine linkages in the main chain; * denotes a urethane or ureido linkage;

a is at least 1;

A denotes a divalent polymeric radical of formula (VI):

wherein:

each R^s independently denotes an alkyl or fluoro-substituted alkyl group having 1 to 10 carbon atoms which may contain ether linkages between carbon atoms;

m is at least 1; and

p provides a moiety weight of 400 to 10,000; each of E and E' independently denotes a polymerizable unsaturated organic radical

represented by formula (VII):

wherein:

R¹² is hydrogen or methyl;

R¹³ is hydrogen, an alkyl radical having 1 to 6 carbon atoms, or a -CO-Y-R¹⁵ radical wherein Y is -O-, -S- or -NH-;

R¹⁴ is a divalent alkylene radical having 1 to 10 carbon atoms;

R¹⁵ is a alkyl radical having 1 to 12 carbon atoms;

X denotes -CO- or -OCO-;

Z denotes -O- or -NH-; Ar denotes an aromatic radical having 6 to 30 carbon atoms;

w is 0 to 6;

x is 0 or 1;

y is 0 or 1; and

z is 0 or 1.

A preferred urethane monomer is represented by formula (VIII):

wherein R¹⁶ is a diradical of a diisocyanate after removal of the isocyanate group, such as the

diradical of isophorone diisocyanate, and each E" is a group represented by:

The silicone-containing monomers may be

copolymerized with a wide variety of hydrophilic monomers to produce silicone hydrogel lenses.

Suitable hydrophilic monomers include: unsaturated carboxylic acids, such as methacrylic and acrylic acids; acrylic substituted alcohols, such as 2-hydroxyethylmethacrylate and 2-hydroxyethylacrylate; vinyl lactams, such as N-vinyl pyrrolidone; and acrylamides, such as methacrylamide and N,N-dimethylacrylamide. Still further examples are the hydrophilic vinyl carbonate or vinyl carbamate monomers disclosed in U.S. Patent Nos. 5,070,215, and the hydrophilic oxazolone monomers disclosed in U. S . Patent No . 4 , 910 , 277. Other suitable

hydrophilic monomers will be apparent to one skilled in the art.

An organic diluent is included in the initial monomeric mixture. As used herein, the term

"organic diluent" encompasses organic compounds which minimize incompatibility of the components in the initial monomeric mixture and are substantially nonreactive with the components in the initial mixture. Additionally, the organic diluent serves to minimize phase separation of polymerized products produced by polymerization of the monomeric mixture. Also, the organic diluent will generally lower the glass transition temperature of the reacting

polymeric mixture which allows for a more efficient curing process, and which ultimately results in a more uniformly polymerized product. Uniformity of the initial monomeric mixture and the polymerized product are of particular concern for silicone hydrogels primarily due to the inclusion of

silicone-containing monomers.

Contemplated organic diluents include:

monohydric alcohols, with C₆-C₁₀ straight-chained aliphatic monohydric alcohols, such as n-hexanol and n-nonanol, being especially preferred; diolε, such as ethylene glycol; polyols, such as glycerin; ethers, such as diethylene glycol monoethyl ether; ketones, such as methyl ethyl ketone; esters, such as methyl enanthate; and hydrocarbons, such as toluene. Preferably, the organic diluent is

sufficiently volatile to facilitate its removal from a cured article by evaporation at or near ambient pressure. Other suitable organic diluents would be apparent to a person of ordinary skill in the art.

The organic diluent is included in an amount effective to provide the desired effect. Generally, the diluent is included at 5 to 60% by weight of the monomeric mixture, with 10 to 50% by weight being especially preferred.

According to the present process, the monomeric mixture, comprising at least one hydrophilic

monomer, at least one silicone-containing monomer and the organic diluent, is cured by conventional methods such as static casting or spincasting.

Subsequently, a sufficient amount of organic diluent is removed from the cured article to improve the machineability of the article. Applicants discovered that although the inclusion of the organic diluent can minimize the aforementioned problems associated with monomer incompatibility, phase separation or nonuniform polymerization, excess residual diluent can render normally soft silicone hydrogel articles even tackier or more rubbery and more difficult to machine; in fact, machining of the cured article may be precluded altogether. Surprisingly, the process according to the present process provides removal of organic diluent from the cured article without deformation of the article, such as warping of the lens.

The organic diluent is preferably removed by evaporation at or near ambient pressure, and an elevated temperature can be employed to shorten the time necessary to evaporate the diluent. The time, temperature and pressure conditions for the removal step will vary depending on such factors as the volatility of the diluent and the specific monomeric components, as can be readily determined by one skilled in the art. According to a preferred embodiment, the temperature employed in the removal step is at least 50°C, and more preferably, at least 55°C. Preferably, the cured article after the diluent removal step will contain no more than 20% by weight of diluent, and preferably, no more than 5% by weight.

Following removal of the organic diluent, the shaped article is machined by various processes known in the art. The machining step includes lathe cutting a lens surface, lathe cutting a lens edge, buffing a lens edge or polishing a lens edge or surface. The present process is particularly advantageous for processes wherein a lens surface is lathe cut, since machining of a lens surface is especially difficult when the surface is tacky or rubbery.

Generally, such machining processes are

performed before the article is released from a mold part. After the machining operation, the lens can be released from the mold part and hydrated.

Alternately, the article can be machined after removal from the mold part and then hydrated. Representative formulations are listed below.

FORMULATION A

Component Parts by Weight

TRIS-VC 55

NVP 30

V2D25 15

VINAL 1

n-nonanol 15

Darocur 0.2

tint agent 0.05

FORMULATION B

Parts by Weight

Component (or Weight Percent)

IDS3H 35

Tris 35

DMA 39

MAA 1

n-hexanol 40

TXN 0.1 %

MDEA 0.2 %

tint agent 0.007 %

FORMULATION C

Parts by Weight

Component for Weight Percent)

IDS3H 30

Tris 30

NVP 27

DMA 9

VDMO 1

HEMAvc 0.15

n-hexanol 30

Darocur 0.5 %

tint agent 0.03 %

FORMULATION D

Parts by Weight

Component for Weight Percent)

IDS3H 30

Tris 30

NVP 27

DMA 9

VDMO 1

HEMAVC 0.15

n-nonanol 30

Darocur 0.5 %

tint agent 0.03 % FORMULATION E

Parts by Weight

Component (or Weight Percent)

IDS3H 35

Tris 35

DMA 48

MAA 1

n-hexanol 40

TXN 0.1 %

MDEA 0.2 %

tint agent 0.007 %

The following materials are designated above.

Darocur Darocur-1173, a UV initiator

DMA N,N-dimethylacrylamide

HEMAvc methacryloxyethyl vinyl carbonate

IDS3H a urethane prepolymer derived from isophorone diisocyanate, diethylene glycol and alpha,omega- bis(hydroxybutyldimethylsilyl) polysiloxane and end-capped with 2- hydroxyethy methacrylate (described in U.S. Patent No. 5,034,461)

MAA methacrylic acid

MDEA methyl diethanolamine

NVP N-vinyl pyrrolidone

tint agent 1,4-bis[4-(2- methacryloxyethyl)phenylamino] anthraquinone

TRIS tris(trimethylsiloxy)silylpropyl methacrylate TRIS-VC tris(trimethylsiloxy)silylpropyl vinyl carbamate

TXN thioxanthone

V₂D₂₅ a silicone-containing vinyl carbonate as previously described

VDMO 2-vinyl-4,4-dimethyl-2-oxazoline-5- one

VINAL N-vinyloxycarbonyl alanine

The following examples further illustrate preferred embodiments of the present invention.

EXAMPLE 1

Under an inert nitrogen atmosphere, 20-μl of Formulation A was injected onto a clean open concave mold made of Barex resin (a rubber modified

copolymer of acrylonitrile and methylacrylate). The mold was spun for about 5 minutes at 320 rpm in the presence of UV light (1-2.5 mW/cm² as measured by Black ray UV meter) and exposed to UV light for about 30 additional minutes to complete the cure.

The lenses were maintained at 60°C for 3 hours in a forced air oven to remove n-nonanol.

Subsequently, the lenses were edged and ball buffed at 1000 rpm for 6 seconds with a force of 25 g while still in the mold. The lenses were manually

released from the molds in water at 50°C, and extracted in isopropanol at room temperature for a minimum of 48 hours. The lenses were then extracted with water at about 85°C for four hours. Finally, the lenses were autoclaved in vials containing buffered saline. EXAMPLE 2

Under an inert nitrogen atmosphere, 30-μl of Formulation B was injected onto a clean open concave Barex resin mold. The mold was spun for about 15 minutes at 341 rpm in the presence of UV light (1-2.5 mW/cm² as measured by Black ray UV meter) and exposed to UV light for about 30 additional minutes to complete the cure.

The lenses were left overnight at room

temperature to remove n-hexanol. Subsequently, the lenses were edged and ball buffed at 1000 rpm for 3 seconds with a force of 130 g while still in the mold. The lenses were released from the molds in an ethanol/water medium, extracted in ethanol at room temperature for a minimum of 48 hours, and then extracted with water at 80°C for 4 hours. Finally, the lenses were cleaned and heat disinfected using unpreserved buffered saline.

EXAMPLE 3

Under an inert nitrogen atmosphere, 45-μl of Formulation C was injected onto a clean Barex resin concave mold half and covered with a polypropylene resin convex mold half. The mold halves were compressed at a pressure of 70 psi and the mixture was cured for about 15 minutes in the presence of UV light (6-11 mW/cm² as measured by Spectronic UV meter), and the mold was exposed to UV light for about 5 additional minutes.

The top mold half was removed and the lenses were maintained at 60°C for 3 hours in a forced air oven to remove n-hexanol. Subsequently, the lens edges were lathe cut and ball buffed for 10 seconds at 2300 rpm with a force of 60 g. The lenses were manually released from the molds in water at 50°C, and then extracted in isopropanol at room

temperature for a minimum of 48 hours, followed by extraction in water at about 85°C for 4 hours.

Finally, the lenses were disinfected using

unpreserved buffered saline.

EXAMPLE 4

Under an inert nitrogen atmosphere, 80-μl of Formulation C was injected onto a clean open concave Barex resin mold. The mold was spun for about 20 minutes at 400 rpm in the presence of UV light (6-10 mW/cm² as measured by Spectronic UV meter) and exposed to UV light for about 12 additional minutes.

The shaped articles were maintained at 60°C for 3 hours in a forced air oven to remove n-hexanol. Subsequently, the posterior surfaces of the articles were lathe cut, then the lenses were polished for 30 seconds. The lenses were manually released from the molds in water at 50°C, extracted in isopropanol for a minimum of 48 hours, followed by extraction in water at about 85°C for 4 hours. Finally, the lenses were autoclaved in buffered saline.

EXAMPLE 5

The procedure of Example 4 was followed except that Formulation D, including 30 parts by weight of n-nonanol, was employed in place of Formulation C. EXAMPLE 6

Each of Formulations X-1, X-2 and X-3

(containing n-hexanol at 10, 15 and 20 parts by weight, respectively) were static cast in flat polypropylene disc molds and cured with UV light. The cured flat discs were inspected. The discs cast from Formulations X-2 and X-3, which contained 15 and 20 parts by weight of n-hexanol, respectively, appeared too tacky to permit machining of the edges due to excess residual n-hexanol, whereas the discs cast from Formulation X-1, which contained only 10 parts by weight of n-hexanol, appeared non-tacky.

FORMULATIONS X-1, X-2, X-3

Parts by Weight

Component for Weight Percent)

IDS3H 35

Tris 35

DMA 30

n-hexanol 10, 15, 20

BME^* 0.2 %

^*BME benzoin methyl ether, a UV initiator

EXAMPLE 7

Lenses were spincast from Formulation A

(containing 15 parts by weight n-nonanol) following the procedure of Example 1. The spincast lenses, remaining in the mold, were placed in a forced air oven maintained at temperatures of 50°C, 55°C and 60°C.

For the lenses dried at 55°C and 60°C, two lenses, remaining in the mold, were removed from the oven at each interval of 0 (control), 1, 2, 3, 4, 5, 6 and 24 hours, and extracted with 2 ml of

isopropanol for a minimum of 12 hours. For the lenses dried at 50°C, two lenses, remaining in the mold, were removed at each interval of 0 (control), 1, 6 and 24 hours, and each sample was extracted with 2 ml of isopropanol for a minimum of 12 hours. Samples of each isopropanol extract (0.1 μl) were obtained and subjected to capillary gas

chromatography to determine n-nonanol content.

The percentage of n-nonanol in the samples, based on the control, was less than 5% after a drying time of 2 hours at 55°C and 60°C and after a drying time of 6 hours at 50°C.

EXAMPLE 8

Lenses were again spincast from Formulation A (containing 15 parts by weight n-nonanol) following the procedure of Example 1. The spincast lenses, remaining in the mold, were placed in a forced air oven maintained at a temperature of 55°C. Ten molds were removed at each interval of 1, 2, 3, 4, 5 and 6 hours and 24 hours (as a control), and the lenses were edged following the procedure of Example 1. The edges of lenses that were maintained at 55°C for 1 hour appeared rough and chipped after edging, whereas the lenses that were maintained at 55°C for 24 hours could be edged satisfactorily. The lenses that exhibited poor edging contained excess residual n-nonanol in the lenses. Each of the lenses that were maintained at 55°C for 2 hours or longer edged comparatively with the lenses maintained at 55°C for 24 hours. Accordingly, sufficient diluent was removed from the spincast lenses to machine edge the lenses by maintaining the lenses at 55°C for at least 2 hours. Based on the data from Example 7, removal of n-nonanol to below 5% was sufficient to provide satisfactory edging.

While certain preferred embodiments have been described, it is understood that the invention is not limited thereto and modifications and variations would be evident to a person of ordinary skill in the art.

Claims

We claim:

1. A process for preparing silicone hydrogel contact lenses, said process comprising:

(a) providing a monomeric mixture comprising a silicone-containing monomer, a hydrophilic monomer and an organic diluent;

(b) charging the monomeric mixture to a mold and curing the formulation in the mold to obtain a shaped article;

(c) removing diluent from the shaped article to improve machineability of the shaped article; and

(d) machining the shaped article to obtain a contact lens having a desired configuration.

2. The process according to claim 1, wherein the monomeric mixture is charged to a mold

comprising a first mold section including a surface for forming an anterior lens surface and a second mold section including a surface for forming a posterior lens surface.

3. The process according to claim 1, wherein the monomeric mixture is cured by spincasting.

4. The process according to claim 1, wherein step (d) comprises machining a lens surface to a desired configuration.

5. The process according to claim 4, wherein the machining comprises lathe cutting a posterior lens surface.

6. The process according to claim 4, wherein the machining comprises lathe cutting an anterior lens surface.

7. The process according to claim 4, wherein the machining comprises polishing a lens surface.

8. The process according to claim 1, wherein step (d) comprises machining an edge of a lens-shaped article to a desired edge configuration.

9. The process according to claim 8, wherein the machining comprises lathe cutting the edge.

10. The process according to claim 8, wherein the machining comprises buffing the edge.

11. The process according to claim 1,

comprising:

(a) providing said monomeric mixture;

(b) charging an excess of said mixture to a mold including a concave surface for forming a desired anterior lens surface and spincast curing the formulation in the mold to obtain a shaped article having the desired anterior lens surface;

(c) removing diluent from the shaped article to improve machineability of the article; and

(d) lathe cutting the posterior surface of the article to obtain a contact lens with a desired thickness.

12. The process according to claim 1,

comprising:

(a) providing said monomeric mixture;

(b) charging said monomeric mixture to a mold, wherein said mold comprises a first mold section including a surface for forming an anterior lens surface and a second mold section including a surface for forming a posterior lens surface, and curing said formulation in the mold to obtain a lens-shaped article having the anterior and

posterior lens surfaces;

(c) removing diluent to improve machineability of the article; and

(d) machining the edge of the article to obtain a contact lens with a desired edge

configuration.

13. The process according to claim 1,

comprising:

(a) providing said monomeric mixture;

(b) charging said monomeric mixture to a mold including a negative molding surface for forming a desired anterior lens surface and spincast curing the monomeric mixture in the mold to obtain a lens-shaped article having the desired anterior lens surface and a desired posterior lens surface;

(c) removing diluent to improve machineability of the article; and

configuration.

14. The process according to claim 1, further comprising hydrating the lens obtained from step (d).

15. The process according to claim 1, wherein the organic diluent is an alcohol.

16. The process according to claim 15, wherein the organic diluent is selected from the group consisting of n-hexanol and n-nonanol.

17. The process according to claim 15, wherein step (c) comprises drying the shaped article at an elevated temperature.

18. The process according to claim 17, wherein the shaped article is maintained at a temperature of at least 50°C for at least 2 hours.

19. The process according to claim 1, wherein the silicone-containing monomer is selected from the group consisting of silicone-containing vinyl carbonate prepolymers and silicone-containing vinyl carbamate prepolymers.

20. The process according to claim 1, wherein the silicone-containing monomer is a silicone-containing urethane prepolymer.

21. A silicone hydrogel contact lens prepared by the process of claim 1.