128 results about "Monoethylene Glycol" patented technology

This invention relates to a method of making a bio-based PET packaging and particularly to a method of producing a bio-based PET from at least one bio-based material comprising: a) forming at least one PET component from at least one bio-based material, wherein the at least one PET component is selected from a monoethylene glycol (“MEG”), a terephthalic acid (“TA”), and combinations thereof; (b) processing said bio-based PET component into a bio-based PET.

Carboxylic acids or the salts thereof are suitable for use in cooling systems where low electrical conductivity is required. The compositions are of particular use in fuel cell stacks. The preferred salts are those of amines. The salts can be used with a liquid alcohol freezing point depressant such as monoethylene glycol. Thiazoles and/or triazoles may be included, as well as other corrosion inhibitors known in the art.

A bottle (1) comprising an envelop (2) defining a housing, said bottle being molded from at least one thermoplastic polymer of at least one FuranDiCarboxylic Acid (FDCA) monomer, preferably 2,5-FuranDiCarboxylic Acid (2,5-FDCA) monomer, and at least one diol monomer, preferably monoethylene glycol (MEG) monomer, wherein the envelop is provided with at least one imprint (10a, 10b).

A MEG reclamation process includes the step of increasing above 2,000 ppm the divalent metal salts concentration of a rich (wet) MEG feed stream flowing into a precipitator. The increasing step includes routing a salts-saturated MEG slipstream from the flash separator it to the precipitator. The slipstream may be mixed with a fresh water feed stream, a portion of the rich MEG feed stream, or some combination of the two. The rich MEG feed stream also may be split into two streams, with a portion of the stream being heated and routed to the flash separator and the other portion being combined as above with the removed slipstream. The process can be performed on the slipstream after dilution and prior to entering the precipitator or after being loaded into the precipitator. Removal of the insoluble salts may be done in either a batch or continuous mode.

This invention discloses one positive light anti-erosion agent peeling agent combination, which comprises the following parts: a, occupying organic amine for weight of 10 to 50; b, monoethylene glycol monoalkyl ether for weigth of 0 to 70 percent; c, non photon electrode solvent for weight of 20 to 90; d, based on the said three component total weight for 0.01 to 10 non-ion surface active agent. This invention relates to positive light anti-erosion peel agent combination to etch process with excellent solve property and peeling property of pattern film for light resistance.

The present invention provides methods, compositions and devices for stabilizing the extracellular nucleic acid population in a cell-containing biological sample using a poly(oxyethylene) polymer or mono-ethylene glycol as stabilizing agent.

The invention is a cement grinding aid, which is made by adding propylene glycol, monoethylene glycol, trolamine, diethylene glycol, urea, soda to the filtered sulphite liquor. The cement grinding aid not only can help improve output of cement, but also effectively limit temperature of a ball grinder in the normal range during cement production; the cement grinding aid further helps maintain normal operation of the ball grinder, and prevent a huge amount of dust and environmental pollution.

The invention concerns a flexible process for purifying a solvent which inhibits the formation of hydrates during gas processing, in particular monoethylene glycol (MEG), said solvent having a boiling point which is higher than that of water and, at least at one point in time, being mixed with water and salts, the process operating in a different manner with the same facility as a function of the quantity of salts in the MEG to be treated. The process operates in accordance with a phase known as reclaiming (separation of salts under vacuum followed by vacuum distillation) when the salts content exceeds the precipitation threshold and if not, the process operates in a regeneration phase (absence of separation of salts and no operation under vacuum). Advantageously, the change is made under the control of means for testing the salts.

A process and an apparatus for the separation of a homogeneous catalyst solution from crude monoethylene glycol (MEG) and for purifying MEG is disclosed. The process comprises separating catalyst solution by evaporating crude MEG and feeding crude MEG to a rectification section, a stripping section, and thence to a pasteurisation section, each section operated at subatmospheric pressure of 0.5×10⁵ Nm⁻² or less, the rectification and pasteurisation sections being at pressure less than that of the catalyst separation section, wherein the process provides a pressure differential across the catalyst separation and rectification sections and wherein vapour phase crude MEG from the catalyst separation section is fed as substantially vapour phase feed to the rectification section. The apparatus comprises a catalyst separation section, an MEG rectification section, a stripping section and a pasteurisation section, wherein the MEG rectification and pasteurisation sections are located within a MEG purification column, and the catalyst separation section is either located in the MEG purification column or in a separate upstream vessel, and wherein the separation section provides a crude MEG feed inlet to the MEG rectification section and an outlet for separated catalyst, wherein the crude MEG feed inlet to the MEG rectification section is a vapour feed inlet.

A liquid crystal aligning agent suitable for use in the production of a liquid crystal display device is provided. The liquid crystal aligning agent comprises at least one polymer selected from a polyamic acid and a soluble polyimide, an aprotic polar solvent and monoethylene glycol dimethyl ether or dipropylene glycol dimethyl ether. The liquid crystal aligning agent has satisfactory printability. Further provided is a liquid crystal alignment layer formed using the aligning agent. The liquid crystal alignment layer is highly uniform.

The present invention relates to a method for producing ethylene alcohol by a catalyzing and distilling method, which is to solve the problems in the existing technology that: the existing method needs multi towers or multi reaction devices and steps to realize the reaction and separation; besides the benefit ratio for non-phase catalyzing single ethylene alcohol is much lower. The present invention adopts water and ethylene oxide as the material, and takes the reaction and separation operations in a catalyzing and distilling tower; so the two processes including the hydration reaction for ethylene oxide and the separation reaction for the ethylene alcohol. The catalyzer used in the present invention adopts an acidic or alkaline organic material or inorganic material or the composite material; the method can solve the problem greatly, which can be uses in the industrial production of ethylene alcohol.

The invention provides a process for the preparation of monoethylene glycol from sucrose comprising the steps of: i) hydrolysing sucrose to form a reaction product stream comprising glucose and fructose; ii) separating the reaction product stream comprising glucose and fructose into a fructose or fructose derivative rich stream and a glucose rich stream; and iii) contacting the glucose rich stream with hydrogen in a reactor in the presence of a solvent and a catalyst system with catalytic hydrogenation abilities to produce a product stream comprising monoethylene glycol.

Monoethylene glycol (MEG) may be reclaimed by a process that includes contacting a MEG-water-salt stream with a heat transfer fluid and then flash separating the MEG and water in the flash separator vessel where the pressure is higher than 0.3 barA (0.03 MPa), the temperature is in the range of above 120° C. to about 250° C., and the residence time of the MEG and water ranges from about 1 second to about 10 minutes, and then removing the MEG and water in an overhead of the flash separator vessel and removing the salt from the flash separator vessel. In some embodiments it is expected that the temperature of the process may range from above 165° C. to about 250° C. and/or that the pressure may be atmospheric.

A system and process for removing hydrocarbons and divalent cations from a rich MEG feed stream is presented. A hydrocarbon removal bed containing a solid adsorbent material adsorbs the hydrocarbons in the rich MEG feed stream as it passes through the hydrocarbon removal bed. After the hydrocarbons have been removed, the rich MEG feed stream flows through an ion exchange bed containing an ion exchange resin in order to remove divalent cations. The rich MEG feed stream then flows through a flash separator and a distillation column to reclaim MEG. Spent solid adsorbent material in the hydrocarbon removal beds and spent ion exchange resin in the ion exchange beds may be regenerated in place using by-products of the MEG reclamation process.

A polyurethane foam, suitable for shoe soles in particular, and a process to prepare it. This polyurethane has a touch that is similar to that of thermoplastic styrene-butadiene-styrene rubber, but offers reduced cost and easy processability. It is prepared from a formulation including a polyether triol with a hydroxyl value of from 25 to 30 and a molecular weight from 5000 to 7000 g/mol; a polyether diol with a hydroxyl value of from 25 to 30 and a molecular weight from 3000 to less than 5000 g/mol; from 2 to 7 wt% of monoethylene glycol, butanediol, hexanediol or neopentyl glycol as a chain extender; a copolymer polyether polyol having a styrene acrylonitrile solids content of at least 30 wt% and an average hydroxyl number of at least 18; an isocyanate component; and a blowing agent that includes water.