WO2004104143A1

WO2004104143A1 - Nitrogen rejection from condensed natural gas

Info

Publication number: WO2004104143A1
Application number: PCT/EP2004/002257
Authority: WO
Inventors: Adam Adrian Brostow; Mark Julian Roberts; Christopher Geoffrey Spilsbury
Original assignee: Air Products and Chemicals Inc
Current assignee: Air Products and Chemicals Inc
Priority date: 2003-05-22
Filing date: 2004-03-05
Publication date: 2004-12-02
Anticipated expiration: 2005-11-22
Also published as: EP2275520A1; KR20060015614A; JP2005043036A; JP2009041017A; US20040231359A1; KR100750578B1; RU2337130C2; MXPA05012494A; RU2005140104A; CN101407736A; CA2523619C; JP4607990B2; CN1572863A; CA2523619A1; JP4216765B2; JP2009052876A; WO2004104143A9; EP1627030A1; AU2004241309A1; NO20042098L

Abstract

Method for the rejection of nitrogen from condensed natural gas which comprises (a) introducing the condensed natural gas into a distillation column at a first location therein, withdrawing a nitrogen-enriched overhead vapor stream from the distillation column, and withdrawing a purified liquefied natural gas stream from the bottom of the column; (b) introducing a cold reflux stream into the distillation column at a second location above the first locatino, wherein the refrigeration to provide the cold reflux stream is obtained by compressing and work expanding a refrigerant stream comprising nitrogen; and (c) either (1) cooling the purified liquefied natural gas stream or cooling the condensed natural gas stream or (2) cooling both the purified liquefied natural gas stream and the condensed natural gas stream, wherein refrigeration for (1) or (2) is obtained by compressing and work expanding the refrigerant stream comprising nitrogen. The refrigerant stream may comprise all or a portion of the nitrogen-rich vapor stream from the distillation column.

Description

SKIN TREATMENTS

Field of the invention

The invention relates to compositions containing activators of the nuclear liver X receptor (LXR) for use in promoting expression of genes involved in dermal regeneration, such as decorin and fibronectin.

Background to the invention Skin is subject to deterioration through dermatological disorders, environmental abuse (wind, air conditioning, central heating) or through the normal ageing process (chronoageing) which may be accelerated by exposure of skin to sun (photoageing). In recent years the demand for cosmetic methods for improving the appearance and condition and, in particular, for reversing, reducing or preventing the visible signs of wrinkled, aged and/or photodamaged skin has grown enormously.

Collagen, the predominant matrix skin protein is known to impart tensile strength to skin. It is also known in the art that the levels of collagen in skin are significantly reduced with aged and/or photodamaged skin. Many studies have shown that the levels of collagen type I in skin are decreased with age and/or with increased photodamage. The reduction of the levels of collagen in skin is accordingly associated with a decrease in the tensile strength of the skin causing wrinkles and laxity.

The small chondroitin sulphate proteoglycan decorin, co-distributes with collagen fibres and is considered essential to the correct formation of newly synthesised collagen fibrils. Studies have also demonstrated that levels of this protein are significantly reduced in aged or photodamaged skin. Likewise fibronectin, a further important component of the dermal extra-cellular matrix which is associated with collagen fibres also reduces with age. It is known that activators of the nuclear liver-X-receptor (LXR) can have a beneficial action on skin epidermal barrier function. LXR activators have been shown previously to induce expression of involucrin and transglutaminase (WO98/32444) and filaggrin (WO03/030857), which are proteins involved in the formation of the epidermal barrier, the stratum corneum. However, the majority of research into LXR has focussed on its role in regulating cholesterol and fatty acid metabolism.

Summary of the invention We have now found that LXR activators exhibit a significant effect on the expression of a number of genes involved in dermal regeneration, notably decorin and fibronectin. Further, we have screened a substantial number of plant extracts and identified a number of extracts that have significant LXR agonist activity.

Accordingly, the present invention provides a method of enhancing decorin and/or fibronectin synthesis in the skin of an animal or human which method comprises administering to said animal or human a nuclear liver X receptor (LXR) activating agent.

In one embodiment, the LXR activating agent comprises a compound according to the general formulae;

(A) or

(B)

wherein;

R represents a hydrogen, a hydroxyl, a keto, an acetyl, a Ci to C-io, substituted or unsubstituted, branched or unbranched, saturated or unsaturated alkyl group.

Ri represents a lower alkyl group, a hydrogen or CORβ;

R₂ represents a hydrogen, a halogen or hydroxyl group;

R₃ represents a hydrogen, a hydroxyl, a halogen, a keto or lower alkyl group;

R₄ represents a hydrogen, a hydroxyl, or a keto group;

R₅ represents a hydrogen, a hydroxyl, a halogen or lower alkyl group;

Re represents a lower alkyl group.

X represents a hydrogen, a methyl or a halogen;

Y represents a hydrogen, a hydroxyl, a acetyl or a keto group;

In another embodiment, the LXR activating agent is a plant extract selected from the group consisting of an extract of Dragon's blood resin (Daemorgos draco), an extract of Damar gum, a non-saponified extract of Nettle (Lamium albim), an extract of Breuzihno resin, an extract of red seaweed, an extract of mastic gum, an extract of mountain ash berry, an extract of plantain leaves and mixtures thereof. The present invention also provides the use of an LXR activating agent in enhancing decorin and/or fibronectin synthesis in the skin of an animal or human.

In a further aspect, the present invention provides a topical composition for enhancing decorin and/or fibronectin synthesis in the skin, said composition comprising;

(a) a plant extract comprising an LXR activating agent, the plant extract being selected from the group consisting of an extract of Dragon's blood resin (Daemorgos draco), an extract of Damar gum, a non-saponified extract of Nettle (Lamium albim), an extract of Breuzihno resin, an extract of red seaweed, an extract of mastic gum, an extract of mountain ash berry, an extract of plantain leaves and mixtures thereof; and

(b) a dermatologically acceptable vehicle.

In a related aspect, the present invention provides a systemic composition for enhancing decorin and/or fibronectin synthesis in the skin, said composition comprising;

(a) a plant extract comprising an LXR activating agent, the plant extract being selected from the group consisting of an extract of Dragon's blood resin (Daemorgos draco), an extract of Damar gum, a non-saponified extract of Nettle (Lamium albim), an extract of Breuzihno resin, an extract of red seaweed, an extract of mastic gum, an extract of mountain ash berry, an extract of plantain leaves and mixtures thereof.

(b) a pharmaceutically acceptable vehicle.

In a further aspect, the LXR activating agents can be used to promote collagen formation in the skin of an animal or human. Detailed Description of the Invention

Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art.

LXR activating agents

Any reference herein to an activator of LXR includes a reference to an activator of LXRσ and/or of LXR/?, unless specifically stated to the contrary.

The LXR activating agents can be provided as pure or semi-pure compounds or as crude extracts of natural products, such as plant extracts.

One preferred class of LXR activating agents comprises the compounds according to the general formulae;

(A) or

(B) wherein;

R represents a hydrogen, a hydroxyl, a keto, an acetyl, a C-i to Cι₀, substituted or unsubstituted, branched or unbranched, saturated or unsaturated alkyl group;

Ri represents a lower alkyl group, a hydrogen or CORβ; R₂ represents a hydrogen, a halogen or a hydroxyl group; R₃ represents a hydrogen, a hydroxyl, a halogen, a keto or a lower alkyl group; R₄ represents a hydrogen, a hydroxyl, or a keto group;

R₅ represents a hydrogen, a halogen, a hydroxyl or lower alkyl group;

R_& represents a lower alkyl group.

X represents a hydrogen, a methyl or a halogen;

Y represents a hydrogen, a hydroxyl, a acetyl or a keto group.

One preferred class of LXR activating compound of formula (A) or (B) is that wherein the R represents -H, -OH, =O, -COCH₃, -COHCH₃, =CHCH₂OH, or -OCOCH₃.

Another possible class of compounds of formulae (A) and (B) wherein R is Ci to Cβ alkyl being substituted or unsubstituted, branched or unbranched and saturated or unsaturated with the proviso that when it is Ca, it is unsaturated.

In formulae A and B, the R group is linked to the carbon at position 17 will depend on the nature of the R group (indicated by wavy bond). Where R is a hydrogen or a hydroxyl group or acetyl group the bond will be saturated, whereas when R is a keto group the bond will be unsaturated. When R is an alkyl group this group may be linked to the carbon at position 17 via a saturated or unsaturated bond, preferably this is an unsaturated bond.

In one preferred sub-class, R represents a hydroxyl, a keto or an acetyl group. R may also represent a Ci to C₇ (i.e. including C_{1 F} C₂, C₃, C₄, C5, Cβ and C₇) substituted or unsubstituted, saturated or unsaturated, branched or unbranched alkyl group. Preferably said Ci to C₇ alkyl group comprises at least one substituted group selected from hydroxyl, keto and acetyl groups and R may in particular represent substituted alkyl groups having two and three of said substitutions. More preferably the alkyl groups have undergone substitution with one or more keto or hydroxyl groups. Further preferred an alkyl R group is substituted at one or more positions corresponding or equivalent to C₂o, C₂ι, C₂₂ and C₂₃ shown in figure 7. Where the substitution is with a keto group this is most preferably bonded to C₂o, whereas when substitution is with a hydroxyl group this is most preferably bonded to a carbon at C₂ι and /or C₂2-

It is preferred that the alkyl R group remains unbranched as this helps to maintain a favoured linear configuration, however in the event that the alkyl group is branch said branches preferably comprise 2 carbons, more preferably 1 carbon.

Where the R group is an alkyl group as described above this will preferably have some degree of unsaturation.

Preferably unsaturation occurs in the form of one or more substituted keto groups.

Where R represents an unsaturated Ci to C₈ alkyl group it is most preferred that this group has the formula -C(CH₃)(CH₂)₂C=C(CH₃)₂.

It appears that the most effective LXR activators of formulae (A) and (B) comprise a small R group. In a preferred embodiment the R group of the LXR activating compound therefore represents a hydrogen, a hydroxyl, a keto or an unsubstituted or, more preferably, substituted C-i to C₄ alkyl group. Preferably substitution occurs at C₂₀ or C₂ι within the alkyl group. Where the R group is an alkyl group it is preferred that this is forms an unsaturated bond with C17 of the ring structure. In a preferred embodiment R represents a hydrogen, a hydroxyl, a keto or a substituted/unsubstituted Ci to C₄ alkyl group. Suitable unsubstituted groups include methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl or ter-butyl.

In a particularly preferred embodiment R is selected from the group consisting of -H, -OH, =O, -COCH₃, -COHCHs, =CHCH₃, =CHCH₂OH, -OCOCH₃ and C(CH₃)(CH₂)₂C=C(CH₃)₂.

A "lower alkyl" as employed herein includes both straight and branched chain radicals of up to four carbon atoms, examples of suitable groups are outlined above. In a preferred embodiment Ri is a hydrogen.

R₂ represents a hydrogen, a halogen preferably chlorine or a hydroxyl group, preferably R₂ represents a hydrogen.

R₃ represents a hydrogen, a halogen preferably a fluorine or chlorine, a keto or a lower alkyl group. Preferably R₃ is either a keto group or a hydrogen. In a most preferred embodiment R₃ is a hydrogen.

Preferably P^ and R₅ represent a hydroxyl group or hydrogen, most preferably these represent a hydrogen.

Re represents a lower alkyl, preferably a methyl group.

X preferably represents a hydrogen, a fluorine or a chlorine, most preferably X is a hydrogen.

Preferably Y represents a hydrogen, a hydroxyl or a keto group.

When Y is a hydrogen, in a compound according to general formula A, a double bond may form between C₁₆ and C-ι₇. In a compound according to formula B, when Y is hydrogen Ri is a preferably hydrogen or -CORβ. Preferably when Y is a keto group the activating molecule conforms to general formula A, whereas, when Y is a hydroxyl group the activating molecule preferably conforms to general formula B.

In a most preferred embodiment the activating compound conforms to formula A wherein Y is a keto group.

Where R is a hydrogen or a hydroxyl group, Y is preferably a keto group in an activating compound according to formula A.

Where R is -COCH₃, Y is preferably a hydrogen or a keto group in a activating compound according to either A or B, preferably according to formula A.

Where R is =CHCH₃ or -OCOCH_3, Y is most preferably a keto group in an activating compound according to general formula A.

Where R is =CHCH₂OH, Y is preferably either; a hydrogen in an activating compound according to general formula A, wherein R is preferably a hydroxyl group; or a hydroxyl group in an activating compound according to formula B wherein Ri is a hydrogen.

Where R is C(CH₃)(CH₂)₂C=C(CH₃)_2, Y is preferably a hydrogen in an activating compound according to formula B wherein R-i is also a hydrogen.

In a preferred embodiment of the use according to the invention the desired activation of LXR is provided by a compound selected from the group consisting of; 4-androsten-3,16-dione, androst-4-ene-3,6,16-trione, 4-androsten-17beta-ol- 3,16-dione acetate, 16-ketotestosterone, 3 ?-acetoxypregna-5,16-dien-20-one, 3 ?-acetoxypregna-5-en-20-one, 3 ?-hydroxypregna-5,16-dien-20-one, 3 ?-hydroxy pregna-5-en-20-one, 5,16-dien-pregnane-3,20-diol, 4,16-dienpregna-3,20-dione, 4,17(20)-(cis)-pregnadien-3,16-dione, 4,17(20)-(trans)-pregnadien-3,16-dione, 4-pregnen-3,16,20-trione, 4,17(20)-pregnadien-11beta,21-diol-3-one, 5,17(20)- pregnadien-3,16-diol-diacetate, 5,17(20)-pregnadien-3,16-diol, 5-pregnen- 3beta,16alpha,21-triol-20-one, 24-hydroxychol-4-en-3-one, cholesta-5,24-dien-3/?- ol, desmosterol, and mixtures thereof.

4,17(20)-(cis)-pregnadien-3,16-dione is particularly preferred.

In one embodiment, dehydroepiandrosterone and its derivatives are specifically excluded.

The preparation of compounds of formulae (A) and (B) has been described in the literature and / or are commercially available e.g. from Sigma Chemical Company.

It is also possible to provide the LXR activator(s) in the form of one or more extracts of natural plant sources, e.g. extracts of one or more of Dragon's blood resin (Daemorgos draco), Damar gum (exudate of Damar tree, Nettle (Lamium albim), red seaweed, Breuzihno resin, mastic gum, mountain ash berry and plantain.

A plant extract differs from the intact plant material in that the various components present in the intact plant material will be present in different amounts in the extract, or substantially absent. Prior to extraction, plant materials may be dried and or mechanically processed, e.g. crushed.

Extracts of plant materials are typically made by solvent extraction. Suitable solvents are those in which LXR activators are soluble. Since LXR activators are typically sterols/steroids, suitable solvents include organic solvents such as hexane, chloroform, benzene, petroleum ether, dichloromethane, acetone, ether, diethyl ether, ethyl acetate and mixtures of the above. Solvents may also include alcohols such as methanol, ethanol and isopropyl alcohol and mixtures thereof, optionally mixtures with water. Preferred solvents are those which are acceptable for use in products destined for human or animal use. Plant materials can also be extracted with supercritical liquid CO₂. Extraction methods include batch extraction and soxhlet extraction at temperatures up to the solvent boiling point. Extraction procedures may therefore include a heating step. Solvent extracted components may be subject to further purification/separation steps such as chromatography or fractional distillation. As used herein, "fraction" means any fractioned part of a solvent containing one or more of the active ingredients described above, e.g. obtained by chromatography or by fractional distillation.

Sterols / steroids represent the unsaponifiable fractions (unsaps) of seed oils and extracts. These are components that cannot be converted to soaps (e.g. non fatty acid / glyceride material). In some extracts e.g. from oils, the unsaps can be enriched by a process of saponification. A suitable method is as follows:

The lipid extract (~1g) from e.g. hexane and methanol extractions is refluxed with 2M potassium hydroxide in ethanol for 1 hour. After cooling the mixture is shaken with diethyl ether. The upper solvent layer containing the unsaponifiable fraction is removed and washed twice with water, dried by passing through a column of sodium sulphate and the solvent removed by evaporation under nitrogen at -70°C. This represents the unsaponifiable material (e.g. sterols).

Formulations

The amount of LXR activator, or mixtures thereof, present in the final composition according to the invention will typically be from 0.001 to 50 wt%, preferably from 0.01 to 10 wt%, and most preferably from 0.1 to 10 % or from 1 to 10 wt% of said composition. The composition is typically formulated for topical application or systemic application.

In one embodiment, the compositions do not contain retinoic acid or a metabolic precursor thereof. Topical formulations

A dermatologically acceptable vehicle acts as a dilutant, dispersant or carrier for the newly identified activators of LXR in the composition, so as to facilitate its distribution when the composition is topically applied.

Dermatologically acceptable vehicles other than water can include liquid or solid emollients, solvents, humectants, thickeners and powders. Examples of each of these types of vehicle which can be used singly or as mixtures of one or more vehicles, are as follows:

Emollients, such as stearyl alcohol, glycerol monoricinoleate, glycerol monostearate, mink oil, cetyl alcohol, isopropyl isostearate, stearic acid, isobutyl palmitate, isocetyl stearate, oleyl alcohol, isopropyl luarate, hexyl laurate, decyl oleate, octadecan-2-ol, isocetyl alcohol, eicosanylalcohol, behenyl alcohol, cetyl palmitate, silicone oils such as dimethylpolysiloxane, di-n-butyl sebacate, isopropyl myristate, isopropyl palmitate, isopropyl stearate, butyl stearate, polyethylene glycol, triethylene glycol, lanolin, cocoa butter, corn oil, cotton seed oil, tallow, lard, olive oil, palm kernal oil, rapeseed oil, safflower seed oil, evening primrose oil, soybean oil, sunflower seed oil, avocado oil, olive oil, sesame seed oil, coconut oil, arachis oil, castor oil, acetylated lanolin alcohols, petroleum jelly, mineral oil, butyl myristate, isostearic acid, palmitic acid, isopropyl linoleate, lauryl lactate, myristyl lactate, decyloleate, myristyl myristate;

Propellants such as trichlorofluoromethane, dichlorodifluoro- methane, dichlorotetrafluoroethane, monochlorodifluoromethane, trichlorotrifluoroethane, propane, butane isobutanem demethyl ether, carbon dioxide, nitrous oxide;

Solvents such as ethyl alcohol, methylene chloride, isopropanol, acetone, ethylene glycol monoethyl ether, diethlyene glycol monobutyl ether, diethylene glycol monoethyl ether, dimethyl sulphoxide, dimethyl formamide, tetrahydrofuran;

Powders, such as chalk, talc, fullers earth, kaolin, starch, gums, colloidal silica sodium polacrylate, tetre alkyl and/or trialkyl aryl ammonium smectites, chemically modified magnesium aluminium silicate, organically modified montmorillonite clay, hydrated aluminium silicate, fumed silica, carboxyvinyl polmer, sodium carboxymethyl cellulose, ethylene glycol monostearate.

The dermatologically acceptable vehicle will usually form from 10 to 99.99 % wt, preferably from 50 to 99 % of the final composition ready for use by the consumer.

The composition may also comprise water, usually up to 98 % volume, preferably 5 to 80 % volume of said final composition.

A topical or skin composition of the invention can be formulated as a lotion having a viscosity of from 4,000 to 10,000 mPas, a fluid cream having a viscosity of from 10,000 to 20,000 mPas or a cream having a viscosity of from 20,000 to 100,000 mPas or above at a temperature of 20°C. The composition may be packaged in a container to suit its viscosity and intended use by the consumer. For example a lotion or fluid cream can be packaged in a bottle or a roll-ball applicator or a propellant driven aerosol device or a container fitted with a pump suitable for finger operation. When the composition is a cream, it can simply be stored in a non-deformable bottle or a squeeze container, such as a tub or a lidded jar.

As already mentioned, compositions of the invention for topical application include personal wash compositions such as liquid soaps, solid soaps, gels, and oils for washing in either the bath or in a shower or for use as a skin moisturising or conditioning product in shower or bath. The invention accordingly also provides a closed container containing a cosmetically acceptable composition as herein defined.

The present invention relates to methods of enhancing or promoting decorin and/or fibronectin production in the skin of a mammal, typically a human. The present invention also relates to methods of promoting collagen formation as a result of the increases in decorin and/or fibronection expressed resulting from administration of LXR activating agents. In one embodiment, such methods comprise the administration of a safe and effective amount of a composition of the invention to the skin or regions thereof. The amount of active agent and frequency of application will vary depending on the initial condition of the skin and the desired end result.

A safe and effective amount of active in a topical composition is applied, generally from about 1 μg to about 1 mg per cm² skin per application, preferably from about 2 g to about 800 μg/cm² skin per application, more preferably from about 30 μg to about 700 /g/cm² skin, most preferably from about 75 μg to about 250 μg/cm² skin. Frequency of application typically ranges from about four times a day to about twice a week, more preferably from about three times a day to about once every other day, more preferably at least twice daily. It is generally preferred that at least one application occurs in the evening.

Systemic formulations

A composition according to the present invention for systemic administration may for example be adapted for oral administration, e.g. in the form of a tablet, lozenge, capsule, liquid (e.g syrup or linctus) or as an injection (e.g. subcutaneous or intramuscular ) or infusion or as a suppository. Typical such formulation techniques and appropriate pharmacologically/pharmaceutically acceptable carriers are well known to those skilled in the art. Suitable compositions for oral administration include those adapted for delayed release and/or for release in the lower gastrointestinal tract.

The amount of the compound administered depends upon the bioavailability of the compound from the composition, in particular where oral administration is used. Typically, however, the LXR activating agents are dosed in an amount of from about 0.01 mg/kg of body weight to about 100 mg/kg, preferably from about 0.1 to about 30 mg/kg of body weight. The amount of the composition depends upon the percent of compound within its formula, which is a function of the amount of the compound required per dose, its stability, release characteristics and other pharmaceutical parameters. The doses are typically administered from once or twice weekly to one or twice daily. The routes of administration and dosages described are intended only as a guide since a skilled practitioner will be able to determine readily the optimum route of administration and dosage for any particular individual.

Another means of systemic dosing comprises dosing any of the aforementioned compositions in a food product which therefore does not necessarily require use of a pharmacologically/pharmaceutically acceptable carrier.

As used herein, the term "food products" includes both food products as such and beverages. Suitable food products as such include spreads, dairy products (including milk and yoghurts), desserts, convenience foods/snacks, breakfast cereals and cereal bars, ready-cook meals, bread and frozen confections such as ice creams, water ices and sorbets and yoghurt ice creams. Food products also include dietary/nutritional supplements. Suitable beverages include tea, tea- flavoured drinks, coffee, soft drinks (e.g. carbonated squashes etc) and fruit juice.

The food products are typically supplemented with the active ingredients of the invention so that they contain higher amounts of the active ingredient(s) than they would normally contain.

The present invention will now be described further with reference to the following examples which are illustrative only and non-limiting.

Example 1 - Gene Expression Analysis of LXR Agonist Effects in Dermal Fibroblasts

Materials and Methods

Cell Culture

For these experiments, skin fibroblasts were isolated from human foreskin. On arrival the skin was stored in holding media DMEM (Dulbecco's Modified Eagles Medium: 2mM L-glutamine, 5 lU/ml penicillin and 5 μg/ml streptomycin, and nystatin 2 mg/ml) at 4°C for several hours. The skin was then cut into 3 x 3 mm squares and transferred into a sterile petri dish, epidermis side up. A 0.2 % filtered dispase solution is added to cover the skin and then the dish sealed and placed at 4°C overnight.

To isolate the fibroblast cells from the skin, the skin samples are removed from the dispase solution and the epidermis peeled off and discarded. The dermis is cut into 1 x 1 mm squares and transferred into a well of a tissue culture plate. A cover slip is placed over the tissue and 1 ml DMEM containing 10% Fetal Calf Serum (FCS), 2mM L-glutamine, 5 lU/ml penicillin and 5 μg/ml streptomycin is added. This was then incubated at 37°C and the growth media changed at 3-4 day intervals until the fibroblasts are approximately 70% confluent. Sterile forceps were used to lift the cover slips, turning them over and placing them cell side up into spare wells. Fresh growth media is added to all of the wells and the cells cultured until, again, the cells were 70% confluent.

To treat the fibroblasts with ligands of LXR, the fibroblasts were plated out at an approximate seeding density of 7000 cells/cm² in DMEM with 10% FCS. All cultures were maintained in a humidified incubator with 5% CO₂ at 37°C and early passage cultures (l-V) were used throughout. Media was then changed to low serum (-1% FCS) 24 hours post seeding and the LXR agonists, 22(R)-hydroxycholesterol or 4, 17-cis-pregnadien-dione, were added in fresh DMEM (+1 % FCS, 0.1 % ethanol) and incubated on the cells for 24 hours. After the treatment, the media was removed and the cells immediately frozen in an ethanol dry ice bath.

RNA extraction and Analysis

To extract RNA from the cultured fibroblasts, the Qiagen RNeasy methodology was used. Frozen fibroblasts were taken from a -20°C freezer and placed in a Class 1 fume hood, and 350μl of Qiagen RNeasy RLT lysis buffer was applied to each plate well whilst the cells were still frozen. The manufacturer's protocol was then followed, and the RNA eluted from the columns with 2 X 50 μl of RNase free water. The samples were then DNased (Ambion) at 37°C for 1 hour using 6 U of DNase enzyme and 5 U of SUPERASE (Ambion). The quality of the RNA was then checked on a non-denaturing 1 % agarose gel. Visualisation of the intensity of the 28 S and 18 S ribosomal RNA bands was used to judge RNA degradation (28S being twice as bright for good quality RNA). The RNA was then precipitated using 0.1 volumes of Ammonium Acetate, and 2 volumes of ethanol. Precipitates were then stored at -20°C in 70 % ethanol.

Before using the RNA in a cDNA synthesis reaction, the quantity of total RNA used in each reaction was assessed using the RiboGreen RNA Quantitation Reagent And Kit (Molecular Probes).

Gene Array

A cDNA array containing 2045 individual clones was used to interrogate the levels of mRNA in the fibroblasts. Standard PCR conditions were used to amplify the cDNA inserts from various plasmid clones. The PCR products were checked on a 1 % agarose ethidium bromide gel and then each one fixed onto Corning Gap II micro-slides in triplicate. Each slide batch was Quality Controlled for spot morphology using SYBR Green II dye (Molecular Probes).

Fluorescent labelling and Array Hybridisation

To get fluorescently labelled cDNA from the RNA, the Genisphere 3DNA Array 350 RP™ expression array detection kit was used. The manufacturer's instructions were followed, except that: 1 ) Powerscript (Clontech) was used for reverse transcription. 2) Cotl DNA was added at a 0.1 concentration to the total RNA.

3) Washing was carried out for 1 x 10 minute in 2 x SSC, 0.2% SDS at 50°C, 2 x

5 minute 2 x SSC at room temperature, and finally 3 x 5 minute in 0.2 x SSC at room temperature.

Array Data Analysis

To get an image and then measure the intensity of fluorescence on each spot, the slides were analysed using a ScanArray 4000XL laser scanner (Packard Biosciences) and the Scan Array image software. Once an image was created, it was analysed using the software package GenePix M (Axon), and the intensity scores for each spot saved in excel. The median background values were subtracted from the mean spot values and then these values exported into GeneSpring™ 4.2 (Silicon Genetics) for analysis. The data was normalised using the 50^th percentile and the Lowess normalisation algorithm.

Results

The expression of a number of genes changed between the vehicle treated cells (0.1% ethanol) and the LXR agonist treated cells. In particular the table below outlines the genes known to be involved in dermal regeneration, and, therefore, likely to influence how skin ages. As each cDNA is spotted in triplicate the ranges of the ratios are shown in brackets.

These results show for the first time that LXR activators increase the levels of expression of genes involved in dermal regeneration such as decorin and fibronectin. This would indicate that LXR activators can be used to promote collagen formation. Example 2 - Screening of plant extracts for LXR agonist activity

Materials and Methods

Nettle (Lamium albim) non-saps extract

This was soxhlet extracted using methanol and the extract was saponified to separate any saps from the unsaps (nonsaps) - as described above.

Dragon's Blood Resin (Daemonorops draco) extract This was an acetone extract of resin purchased from Frontier Natural Products Co-operative, Norway, Indiana, US.

Damar gum extract

This was an ethyl acetate extract of resin purchased from Thew Arnott Ltd., Surrey, UK.

Red seaweed extract

Hexane extracts were prepared of the seaweed material.

Breuzihno resin extract

This was soxhlet extracted using methanol, from a sample purchased from Nahziryah Monastic Community's on-line services, Saint Joe, Arizona, US.

mastic gum extract This was soxhlet extracted using methanol, from a sample of mastic gum purchased commercially. Mastic gum is a natural resin from the Pistacia lentiscus tree (an evergreen shrub from the pistachio tree family), which is found on the Island of Chios in Greece. Available commercially as, for example, Mastika, Natural Chios Mastic Gum.

mountain ash berry extract

This was purchased from Molecular Nature Limited (MNL) who used a soxhlet extraction (dichloromethane) followed by a cleanup to remove excess fats and chlorophyll. The extract was subjected to normal phase flash chromatography using a hexane:ethyl acetate:methanol gradient system on Flash 75 Biotage columns. The fractions were then sub-fractionated using semi preparative reverse phase chromatography using a gradient of water with increasing amounts of acetonitrile and then washing with acetone.

plantain leaf extract

This was purchased from Molecular Nature Limited (MNL) who used the same soxhlet extraction (dichloromethane) procedure and fractionation method described above for mountain ash berries.

Over 400 compounds or plant extracts were screened for their ability to activate LXR using the LXRσ reporter gene assay described in WO03/030857.

Compounds/extracts which showed a fold-activation over the control of 1.9 or more were selected and are listed below:

Example 3

The formulation below describes an emulsion cream for use according to the present invention.

Wt %

Example 4

The formulation below describes an oil in water cream suitable for the methods and uses according to the present invention. The percentages indicated are by weight of the composition.

* Brij 56 is cetyl alcohol POE (10) ** Alfol 16RD is cetyl alcohol

Example 5

The formulation below described a soup composition suitable for the methods and uses according to the present invention.

3.4 grams of vegetable fat}

0.5 grams of modified egg yolk} together named "creamer"

6.0 grams of maltodextrin}

1.0 grams of Red Seaweed extract

0.6 grams of maize starch croutons

16.1 grams of dried potato starch

1.0 grams of salt

0.3 grams of onion solids

0.7 grams of onions

0.2 grams of parsley and herb extract

3.2 grams of flavouring agents The creamer and the other component are mixed in a mixer. The blend obtained is a dried instant onion soup that can be used for making a soup by mixing it with 200 ml of boiling water under stirring.

The various features and embodiments of the present invention, referred to in individual sections above apply, as appropriate, to other sections, mutatis mutandis. Consequently features specified in one section may be combined with features specified in other sections, as appropriate.

All publications mentioned in the above specification are herein incorporated by reference. Various modifications and variations of the described methods and products of the invention will be apparent to those skilled in the art without departing from the scope of the invention. Although the invention has been described in connection with specific preferred embodiments, it should be understood that the invention as claimed should not be unduly limited to such specific embodiments. Indeed, various modifications of the described modes for carrying out the invention which are apparent to those skilled in the relevant fields are intended to be within the scope of the following claims.

Claims

1. A method of enhancing decorin and/or fibronectin synthesis in the skin of an animal or human which method comprises administering to said animal or human a nuclear liver X receptor (LXR) activating agent.

2. A method according to claim 1 , wherein the LXR activating agent comprises a compound according to the general formulae;

(A)

or

(B)

wherein; R represents a hydrogen, a hydroxyl, a keto, an acetyl, a Ci to Cι₀, substituted or unsubstituted, branched or unbranched, saturated or unsaturated alkyl group.

Ri represents a lower alkyl group, a hydrogen or CORβ; R₂ represents a hydrogen, a halogen or hydroxyl group; R₃ represents a hydrogen, a hydroxyl, a halogen, a keto or lower alkyl group; R represents a hydrogen, a hydroxyl, or a keto group; R₅ represents a hydrogen, a hydroxyl, a halogen or lower alkyl group; R_δ represents a lower alkyl group.

X represents a hydrogen, a methyl or a halogen;

Y represents a hydrogen, a hydroxyl, a acetyl or a keto group;

3. A method according to claim 2, wherein R represents a hydrogen, a hydroxyl, a keto or a Ci to C substituted or unsubstituted alkyl group.

4. A method according to claim 2, wherein R represents a substituted unbranched Ci to C₄ alkyl group.

5. A method according to any one of claims 2 to 4, wherein said activating compound is according to general formula A, and wherein Y is a keto group.

6. A method according to any one of claims 2 to 4, wherein said activating compound is according to general formula B, and wherein Ri represents a hydrogen and Y represents a hydroxyl group, a hydrogen or an acetyl group.

7. A method according to any one of claims 2 to 6, wherein R represents -H, -OH, =O, -COCH₃, -COHCH₃, =CHCH₃, =CHCH₂OH, or -OCOCH₃

8. Use according to claim 2, wherein R represents C(CH₃)(CH₂)₂C=C(CH₃).

9. A method according to claim 2, wherein said LXR activating agent is a compound selected from the group consisting of 4-androsten-3,16-dione, androst- 4-ene-3,6,16-trione, 4-androsten-17beta-ol-3,16-dione acetate, 16-ketotesto sterone, 3/?-acetoxy pregna-5,16-dien-20-one, 3 ?-acetoxypregna-5-en-20-one, 3 ?-hydroxypregna-5,16-dien-20-one, 3β-hydroxypregna-5-en-20-one, 5,16-dien- pregnane-3,20-diol, 4,16-dienpregna-3,20-dione, 4,17(20)-(cis)-pregnadien-3,16- dione, 4,17(20)-(trans)-pregnadien-3,16-dione, 4-pregnen-3,16,20-trione, 4,17(20)-pregnadien-11/?,21-diol-3-one, 5,17(20 )-pregnadien-3,16-diol-diacetate, 5,17(20)-pregnadien-3,16-diol, 5-pregnen-3beta,16alpha,21-triol-20-one,

24-hydroxychol-4-en-3-one, cholesta-5,24-dien-3β-ol, (3beta)-3-hydroxyurs-12- en-28oic acid, desmosterol, and mixtures thereof.

10. A method according to claim 1 , wherein the LXR activating agent is a plant extract selected from the group consisting of an extract of Dragon's blood resin (Daemorgos draco), an extract of Damar gum, a non-saponified extract of Nettle (Lamium albim), an extract of Breuzihno resin, an extract of red seaweed, an extract of mastic gum, an extract of mountain ash berry, an extract of plantain leaves and mixtures thereof.

11. A method according to any one of preceding claims wherein the LXR activating agent is administered topically.

12. A method according to any one of preceding claims wherein the LXR activating agent is administered systemically.

13. A method according to claim 12 or claim 13, wherein said LXR activating agent is present in a composition at a level of from 0.1 to 10 % wt of the composition.

14. Use of an LXR activating agent in enhancing decorin and/or fibronectin synthesis in the skin.

15. Use according to claim 14 wherein the LXR activating agent is as defined in any one of claims 2 to 12.

16. Use according to claim 15 wherein the LXR activating agent is provided as a topical composition comprising the LXR activating agent and a dermatologically acceptable vehicle.

17. Use according to claim 15 wherein the LXR activating agent is provided as a systemic composition comprising the LXR activating agent and a pharmaceutically acceptable vehicle.

18. Use according to claim 16 or claim 17 wherein the LXR activating is present in a composition at a level of from 0.1 to 10 % wt of the composition.

8. The method of Claim 7 wherein the purified liquefied natural gas stream is cooled by indirect heat exchange with the nitrogen-enriched overhead vapor stream from the distillation column and the cold nitrogen-rich refrigerant stream to provide a subcooled liquefied natural gas product.

9. The method of Claim 1 wherein the cold reflux stream, refrigeration to provide the cold reflux stream, and refrigeration to cool either (i) the purified liquefied natural gas stream or the condensed natural gas stream or (ii) both the purified liquefied natural gas stream and the condensed natural gas stream are provided by

(1) warming the nitrogen-enriched overhead vapor stream from the distillation column to provide by indirect heat exchange a first portion of the refrigeration to generate the cold reflux stream and to cool either (i) the purified liquefied natural gas stream or the condensed natural gas stream or (ii) both the purified liquefied natural gas stream and the condensed natural gas stream, thereby providing a warmed nitrogen-rich vapor stream;

(2) withdrawing a first portion of the warmed nitrogen-rich vapor stream as a nitrogen reject stream and compressing a second portion of the warmed nitrogen-rich vapor stream to provide a compressed nitrogen-rich stream; (3) combining the compressed nitrogen-rich stream with a warmed work expanded nitrogen-rich stream to provide a combined nitrogen-rich stream and compressing the combined nitrogen-rich stream to provide a combined compressed nitrogen-rich stream;

(4) cooling the combined compressed nitrogen-rich stream to yield a cooled compressed nitrogen-rich stream, work expanding a first portion of the cooled compressed nitrogen-rich stream to yield a cold nitrogen-rich refrigerant stream, and warming the cold nitrogen-rich refrigerant stream to provide by indirect heat exchange a second portion of the refrigeration to generate the cold reflux stream and to cool either (i) the purified liquefied natural gas stream or the condensed natural gas stream or (ii) both the purified liquefied natural gas stream and the condensed natural gas stream, thereby providing the warmed work expanded nitrogen-rich stream; and (5) cooling a second portion of the cooled compressed nitrogen-rich stream by indirect heat exchange with the nitrogen-enriched overhead vapor stream from the distillation column and the cold nitrogen-rich refrigerant stream to provide a cold compressed nitrogen-rich stream, and reducing the pressure of the i cold compressed nitrogen-rich stream to provide the cold reflux stream.

10. The method of Claim 9 wherein the purified liquefied natural gas stream is subcooled by indirect heat exchange with the nitrogen-enriched overhead vapor stream from the distillation column and the cold nitrogen-rich refrigerant stream to provide a subcooled liquefied natural gas product.

11. The method of Claim 9 which further comprises reducing the pressure of the cold compressed nitrogen-rich stream to provide a cold two-phase nitrogen-rich stream, separating the cold two-phase nitrogen-rich stream to yield a cold nitrogen-rich liquid stream and a cold nitrogen-rich vapor stream, reducing the pressure of the cold nitrogen- rich liquid stream to provide the cold reflux stream, and combining the cold nitrogen-rich vapor stream with the cold nitrogen-rich refrigerant stream of (4).

12. The method of Claim 11 which further comprises reducing the pressure of the cold nitrogen-rich vapor stream to provide a reduced-pressure vapor stream and combining the reduced-pressure vapor stream with either the cold nitrogen-rich refrigerant stream of (4) or the nitrogen-enriched overhead vapor stream from the distillation column of (1).

13. The method of Claim 11 wherein a portion of the cold nitrogen-rich liquid stream is vaporized in an intermediate condenser in the distillation column between the first and second locations therein to form a vaporized nitrogen-rich stream, and the vaporized nitrogen-rich stream is combined with the cold nitrogen-rich vapor stream.

14. The method of Claim 9 which further comprises reducing the pressure of the condensed natural gas stream to form a two-phase stream, separating the two-phase stream into a methane-enriched liquid stream and a nitrogen-enriched vapor stream, cooling the methane-enriched liquid stream by indirect heat exchange with the nitrogen- enriched overhead vapor stream from the distillation column and the cold nitrogen-rich refrigerant stream to provide a subcooled condensed natural gas feed stream, further cooling the subcooled condensed natural gas feed stream by indirect heat exchange with a vaporizing liquid withdrawn from the bottom of the distillation column to provide a vaporized bottoms stream, introducing the vaporized bottoms stream into the distillation column to provide boilup vapor therein, cooling the nitrogen-enriched vapor stream by indirect heat exchange with the nitrogen-enriched overhead vapor stream from the distillation column and the cold nitrogen-rich refrigerant stream to provide a cooled natural gas feed stream, and introducing the cooled natural gas feed stream into the distillation column at a point intermediate the first and second location therein.

15. The method of Claim 14 which further comprises subcooling the purified liquefied natural gas stream by indirect heat exchange with the nitrogen-enriched overhead vapor stream from the distillation column and with the cold nitrogen-rich refrigerant stream.

16. The method of Claim 9 wherein, following cooling of the second portion of the cooled compressed nitrogen-rich stream by indirect heat exchange with the nitrogen-enriched overhead vapor stream from the distillation column and the cold nitrogen-rich refrigerant stream and prior to reducing the pressure of the cold compressed nitrogen-rich stream to provide the cold reflux stream, the cold compressed nitrogen-rich stream is further cooled by indirect heat exchange with a vaporizing liquid withdrawn from the bottom of the distillation column, thereby providing a vaporized bottoms stream, and introducing the vaporized bottoms stream into the distillation column to provide boilup vapor therein.

17. The method of Claim 1 wherein the cold reflux stream, refrigeration to provide the cold reflux stream, and refrigeration to cool either (i) the purified liquefied natural gas stream or the condensed natural gas stream or (ii) both the purified liquefied natural gas stream and the condensed natural gas stream are provided by (1 ) warming a cold nitrogen-rich vapor stream to provide a first portion of refrigeration to provide the cold reflux stream and refrigeration to cool either (i) the purified liquefied natural gas stream or the condensed natural gas stream or (ii) both the purified liquefied natural gas stream and the condensed natural gas stream, thereby providing a warmed nitrogen-rich vapor stream;

(2) compressing the warmed nitrogen-rich vapor stream to provide a compressed nitrogen-rich stream; (3) combining the compressed nitrogen-rich stream with a warmed work expanded nitrogen-rich stream to provide a combined nitrogen-rich stream and compressing the combined nitrogen-rich stream to provide a combined compressed nitrogen-rich stream;

(4) cooling the combined compressed nitrogen-rich stream to yield a cooled compressed nitrogen-rich stream, work expanding a first portion of the cooled compressed nitrogen-rich stream to yield a cold nitrogen-rich refrigerant stream, and warming the cold nitrogen-rich refrigerant stream to provide a second portion of refrigeration to cool either (ii) the purified liquefied natural gas stream or the condensed natural gas stream or (ii) both the purified liquefied natural gas stream and the condensed natural gas stream, thereby providing the warmed work expanded nitrogen-rich stream of (3);

(f) cooling a second portion of the cooled compressed nitrogen-rich stream by indirect heat exchange with the cold nitrogen-enriched overhead vapor stream and the cold nitrogen-rich refrigerant stream to provide a cold compressed nitrogen-rich stream, and reducing the pressure of the cold compressed nitrogen- rich stream to provide a cold nitrogen-rich refrigerant stream; and

(g) partially condensing overhead vapor from the distillation column in the overhead condenser by indirect heat exchange with the cold nitrogen-rich refrigerant stream tojorm a two-phase overhead stream and the nitrogen-rich vapor stream of (1), separating the two-phase overhead stream into a vapor portion and a liquid portion, returning the liquid portion to the distillation column as the cold reflux stream, and withdrawing the vapor portion as a nitrogen reject stream.

18. A method for the rejection of nitrogen from condensed natural gas which comprises

- (a) introducing a condensed natural gas feed into a distillation column at a first location therein, withdrawing a nitrogen-enriched overhead vapor stream from the distillation column, and withdrawing a purified liquefied natural gas stream from the bottom of the column; and

(b) introducing a cold reflux stream into the distillation column at a second location above the first location, wherein the cold reflux stream and refrigeration to provide the cold reflux stream are obtained by steps which comprise compressing all or a portion of the nitrogen-enriched overhead vapor stream to , provide a compressed nitrogen-enriched stream, work expanding a portion of the compressed nitrogen-enriched stream to generate the refrigeration to provide the cold reflux stream, and cooling and reducing the pressure of another portion of the compressed nitrogen-enriched stream to provide the cold reflux stream.

19. The method of Claim 18 wherein the condensed natural gas feed to the distillation column is provided by cooling condensed natural gas by indirect heat exchange with a vaporizing liquid withdrawn from the bottom of the distillation column to provide a vaporized bottoms stream, and introducing the vaporized bottoms stream into the distillation column to provide boilup vapor therein.

20. The method of Claim 18 wherein the cold reflux stream and refrigeration to provide the cold reflux stream are provided by (a) warming the nitrogen-enriched overhead vapor stream from the distillation column to provide a first portion of refrigeration to provide the cold reflux stream, thereby providing a warmed nitrogen-rich vapor stream;

(b) withdrawing a first portion of the warmed nitrogen-rich vapor stream as a nitrogen reject stream and compressing a second portion of the warmed nitrogen-rich vapor stream to provide a compressed nitrogen-rich stream;

(c) combining the compressed nitrogen-rich stream with a warmed work expanded nitrogen-rich stream to provide a combined nitrogen-rich stream and compressing the combined nitrogen-rich stream to provide a combined compressed nitrogen-rich stream; (d) cooling the combined compressed nitrogen-rich stream to yield a cooled compressed nitrogen-rich stream, work expanding a first portion of the cooled compressed nitrogen-rich stream to yield a cold nitrogen-rich refrigerant stream, and warming the cold nitrogen-rich refrigerant stream to provide a second portion of the refrigeration to provide the cold reflux stream, thereby providing the warmed work expanded nitrogen-rich stream; and (e) cooling a second portion of the cooled compressed nitrogen-rich stream by indirect heat exchange with the nitrogen-enriched overhead vapor stream from the distillation column and the cold nitrogen-rich refrigerant stream to provide a cold compressed nitrogen-rich stream, reducing the pressure of the cold compressed nitrogen-rich stream to provide a reduced-pressure cold nitrogen-rich stream, and introducing the reduced-pressure cold nitrogen-rich stream into the distillation column as the cold reflux stream.

21. The method of Claim 18 which further comprises reducing the pressure of the condensed natural gas prior to the distillation column by passing the cooled liquefied natural gas feed through a dense-fluid expander.

22. A system for the rejection of nitrogen from condensed natural gas which comprises

(a) a distillation column having a first location for introducing the condensed natural gas, a second location for introducing a cold reflux stream, wherein the second location is above the first location, an overhead line for withdrawing a nitrogen-enriched overhead vapor stream from the top of the column, and a line for withdrawing a purified liquefied natural gas stream from the bottom of the column;

(b) compression means for compressing a refrigerant comprising nitrogen to provide a compressed nitrogen-containing refrigerant;

(c) an expander for work expanding a first portion of the compressed nitrogen-containing refrigerant to provide a cold work-expanded refrigerant;

(d) heat exchange means for warming the cold work-expanded refrigerant and for cooling, by indirect heat exchange with the cold work-expanded refrigerant, a second portion of the compressed nitrogen-containing refrigerant and either (1) the purified liquefied natural gas stream or the condensed natural gas stream or (2) both the purified liquefied natural gas stream and the condensed natural gas stream; and

(e) means for reducing the pressure of a cooled second portion of the compressed nitrogen-containing refrigerant withdrawn from the heat exchange means to provide refrigeration to the distillation column.

23. The system of Claim 22 which comprises piping means to combine the nitrogen- enriched overhead vapor stream and the cold work-expanded nitrogen-rich gas to form a cold combined nitrogen-rich stream, and wherein the heat exchange means comprises one or more flow passages for warming the cold combined nitrogen-rich stream to provide a warmed combined nitrogen-rich stream.

24. The system of Claim 23 wherein the compression means includes a single-stage compressor for compression of the warmed combined nitrogen-rich stream.

25. The system of Claim 22 wherein the heat exchange means comprises a first group of flow passages for warming the nitrogen-enriched overhead vapor stream to form a warmed nitrogen-enriched overhead vapor stream and a second group of flow passages for warming the cold work-expanded refrigerant to form a warmed work-expanded refrigerant.

26. The system of Claim 25 wherein the compression means includes a compressor having a first stage and a second stage, and wherein the system includes piping means to transfer the warmed nitrogen-enriched overhead vapor stream from the heat exchange means to an inlet of the first stage of the compressor and piping means to transfer the warmed work-expanded refrigerant from the heat exchange means to an inlet of the second stage of the compressor.

27. A system for the rejection of nitrogen from condensed natural gas which comprises (a) a distillation column having a first location for introducing the condensed natural gas into the distillation column, a second location for introducing a cold reflux stream into the distillation column, wherein the second location is above the first location, an overhead line for withdrawing a nitrogen- enriched overhead vapor stream from the distillation column, and a line for withdrawing a purified liquefied natural gas stream from the bottom of the column; (b) compression means for compressing all or a portion of the nitrogen- enriched overhead vapor stream to provide a compressed nitrogen-rich vapor stream;

(c) an expander for work expanding a first cooled compressed nitrogen- rich vapor stream to provide a cold work-expanded nitrogen-rich stream; (d) heat exchange means comprising

(d1) a first group of flow passages for warming the cold work-expanded nitrogen-rich stream to provide a warm work- expanded nitrogen-rich stream;

(d2) a second group of flow passages for warming the nitrogen-enriched overhead vapor stream from the distillation column to provide a warm nitrogen-enriched overhead vapor stream;

(d3) a third group of flow passages for cooling the compressed nitrogen-rich vapor stream by indirect heat exchange with the cold work-expanded nitrogen-rich stream and the nitrogen-enriched overhead vapor stream from the distillation column to provide the first cooled compressed nitrogen-rich vapor stream and a second cooled compressed nitrogen-rich vapor stream; and (e) means for reducing the pressure of the second cooled compressed nitrogen-rich vapor stream to provide the cold reflux stream and means for introducing the cold reflux stream into the distillation column at the second location.

28. The system of Claim 27 which further comprises reboiler means for cooling the condensed natural gas prior to introduction into the distillation column by indirect heat exchange with a vaporizing stream withdrawn from the bottom of the distillation column, thereby forming a vaporized stream, and means to introduce the vaporized stream into the bottom of the distillation column to provide boilup vapor therein.

29. The system of Claim 27 wherein the compression means includes a compressor having a first stage and a second stage, and wherein the system includes piping means to transfer the warm nitrogen-enriched overhead vapor stream from the heat exchange means to an inlet of the first stage of the compressor and piping means to transfer the warm work-expanded nitrogen-rich stream from the heat exchange means to an inlet of the second stage of the compressor.