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A LIQUID EXTRACTION SYSTEM AND METHOD THEREOF
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Abstract
Information
Inventors
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Specification
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ORDINARY APPLICATION
Published
Filed on 21 November 2024
Abstract
ABSTRACT The present invention provides a super critical liquid extraction system for the isolation of the phytochemicals. The system of the present invention uses two solvent chambers along with the CO2 chamber connected with the Pump which converted the solvent in to vapor phase and shifted the vapor of the solvent along with the CO2 vapor into the mixer where it converted it into the homogeneous gaseous mixture. and another pump located after the mixer shifted the homogeneous gaseous mixture into the preheated heater where it convert the some remaining liquid component in to the gaseous component as well as homogeneous gaseous mixture will be charged and finally the homogeneous gaseous mixture of the two solvent and CO2 reaches in to the temperature programmed microwave oven which contain the material to be extracted.
Patent Information
Application ID | 202411090336 |
Invention Field | ELECTRICAL |
Date of Application | 21/11/2024 |
Publication Number | 49/2024 |
Inventors
Name | Address | Country | Nationality |
---|---|---|---|
DR. HARISH CHANDRA JOSHI | Department of Chemistry, Graphic Era (Deemed to be University), 566/6, Bell Road, Clement Town, Dehradun – 248002, Uttarakhand, India | India | India |
DR. WASEEM AHMAD | Department of Chemistry, Graphic Era (Deemed to be University), 566/6, Bell Road, Clement Town, Dehradun – 248002, Uttarakhand, India | India | India |
Applicants
Name | Address | Country | Nationality |
---|---|---|---|
GRAPHIC ERA (Deemed to be University) | 566/6 Bell Road, Clement Town, Dehradun - 248002, Uttarakhand, India | India | India |
Specification
Description:FORM 2
THE PATENTS ACT, 1970
(39 OF 1970)
&
THE PATENTS RULES, 2003
COMPLETE SPECIFICATION
(See section 10; rule 13)
Title: A LIQUID EXTRACTION SYSTEM AND METHOD THEREOF
APPLICANT DETAILS:
(a) NAME: GRAPHIC ERA (Deemed to be University)
(b) NATIONALITY: Indian
(c) ADDRESS: 566/6 Bell Road, Clement Town, Dehradun - 248002, Uttarakhand,
India
PREAMBLE TO THE DESCRIPTION:
The following specification particularly describes the nature of this invention and the manner in which it is to be performed.
A LIQUID EXTRACTION SYSTEM AND METHOD THEREOF
Field of Invention:
The present invention relates to an advanced extraction technique for the isolation of phytochemical using a homogeneous gaseous mixture of supercritical liquid.
Background of the Invention.
The following background discussion includes information that may be useful in understanding the present invention. It is not an admission that any of the information provided herein is prior art or relevant to the presently claimed invention, or that any publication expressly or implicitly referenced is prior art.
The principles of supercritical fluid extraction (SFE) have been known since the work of Baron Cagniard de le Tour in 1822 when it was noted that the gas-liquid boundary disappeared when the temperature of certain materials was increased by heating them in a closed glass container. From this early work the critical point of a substance was first discovered. The critical point is the temperature above which a substance can co-exist in gas, liquid and solid phases. It was later found that by taking substances to or above their critical temperature and pressure they could be used as sophisticated solvents for extraction and fractionation of complex mixtures. For example, US11465072B2 discloses a system of and for extraction or removal of phytochemicals from plants, including those of the plant family Cannabaceae sensu stricto. More specifically, a system for extracting essential oils from plants, such as cannabis, without the use of a solvent.
Further, US20030072677A1 discloses methods for preparing tissue for incorporation into xenografts and bioprosthetic devices. The methods of the invention make use of supercritical fluids to remove infectious materials and chemical agents from tissues, as well as to permeate a tissue with a chemical agent (e.g. tanning, cross-linking, and bioactive agents).
In another document, US4493797A discloses an autoclave extraction apparatus using supercritical fluid is used for supercritical fluid extraction of one or several compounds. The supercritical fluid containing the compound(s) may then be processed in a pressurized bed reactor under supercritical conditions. The bed being a fluidizable catalytic bed to carry out a catalytic reaction of the compound(s). The method is particularly applicable to recover valuable lignin and other extractable components from kraft black liquor.
However, none of the cited documents uses an advanced extraction technique for the isolation of phytochemical using a homogeneous gaseous mixture of supercritical liquid. The present invention provides an advanced extraction technique for the isolation of phytochemical using a homogeneous gaseous mixture of supercritical liquid.
Object(s) of the present invention:
The primary objective of the present invention is to overcome the drawback associated with prior art.
An object of the present invention is to provide an advanced extraction technique for the isolation of phytochemical using a homogeneous gaseous mixture of supercritical liquid.
Summary of the Invention:
In an aspect the present invention provides a liquid extraction system for the isolation of the phytochemicals, comprising:
a) at least two solvent chambers along with a CO2 chamber connected with a pump which converts the solvent into vapor phase;
b) a mixer chamber connected to the pump of the solvent chambers and the CO2 chambers where the pumps shift the vapor of the solvent along with the CO2 vapor into the mixer where it converted it into the homogeneous gaseous mixture;
c) an another pump mounted after the mixer chamber is configured to shift the homogeneous gaseous mixture into a preheated heater;
d) a microwave configured to receive homogeneous gaseous mixture which contain a material to be extracted,
wherein in the microwave oven the gaseous mixture comes in contact with a substance and extracts the phytochemicals from the given materials and finally isolated extracted collected into a collector.
In an embodiment, the preheater is configured to converted remaining liquid component into the gaseous component.
In an embodiment, the preheater is also configured to charge the homogeneous gaseous mixture.
In an embodiment, the homogeneous gaseous mixture of the two solvent and CO2 reaches into the temperature microwave oven wherein the microwave oven is programmed for the extraction.
In an aspect the present invention provides a method of operation of liquid extraction system for the isolation of the phytochemicals, comprising:
a) converting two solvents and CO2 together into vapor phase by plurality of pumps;
b) converting the vapor phase into a homogeneous gaseous mixture by a mixer chamber; and
c) sending the homogeneous gaseous mixture obtained at step (b) by a pump into a preheated heater;
wherein in the microwave oven the gaseous mixture comes in contact with a substance and extracts the phytochemicals from the given materials and finally isolated extracted collected into a collector.
Brief description of Drawings:
The accompanying drawings, which are incorporated in and constitute a part of this disclosure, illustrate exemplary embodiments and, together with the description, explain the disclosed principles. The reference numbers are used throughout the figures to describe the features and components. Some embodiments of system and/or methods in accordance with embodiments of the present subject matter are now described, by way of example only, and regarding the accompanying figures, in which
Figure 1: illustrates the system of the present invention.
Detailed description of the invention:
In the present document, the word "exemplary" is used herein to mean "serving as an example, instance, or illustration." Any embodiment or implementation of the present subject matter described herein as "exemplary" is not necessarily to be construed as preferred or advantageous over other embodiments.
While the disclosure is susceptible to various modifications and alternative forms, specific embodiment thereof has been shown by way of example, in the drawings and will be described in detail below. It should be understood, however, that it is not intended to limit the disclosure to the specific forms disclosed, but on the contrary, the disclosure is to cover all modifications, equivalents, and alternative falling within the spirit and the scope of the disclosure.
The terms "comprises", "comprising", "includes", or any other variations thereof, are intended to cover a non-exclusive inclusion, such that a setup, device or method that comprises a list of components or steps does not include only those components or steps but may include other components or steps not expressly listed or inherent to such setup or device or method. In other words, one or more elements in a system or apparatus proceeded by "comprises... a" does not, without more constraints, preclude the existence of other elements or additional elements in the system or method.
In an embodiment, the present invention provides an advanced extraction technique for the isolation of phytochemical using a homogeneous gaseous mixture of supercritical liquid.
In an embodiment, the present invention provides a liquid extraction system for the isolation of the phytochemicals, comprising:
a) at least two solvent chambers along with a CO2 chamber connected with a pump which converts the solvent into vapor phase;
b) a mixer chamber connected to the pump of the solvent chambers and the CO2 chambers where the pumps shift the vapor of the solvent along with the CO2 vapor into the mixer where it converted it into the homogeneous gaseous mixture;
c) an another pump mounted after the mixer chamber is configured to shift the homogeneous gaseous mixture into a preheated heater;
d) a microwave configured to receive homogeneous gaseous mixture which contain a material to be extracted,
wherein in the microwave oven the gaseous mixture comes in contact with a substance and extracts the phytochemicals from the given materials and finally isolated extracted collected into a collector.
In an embodiment, the preheater is configured to converted remaining liquid component into the gaseous component.
In an embodiment, the preheater is also configured to charge the homogeneous gaseous mixture.
In an embodiment, the homogeneous gaseous mixture of the two solvent and CO2 reaches into the temperature microwave oven wherein the microwave oven is programmed for the extraction.
In an aspect the present invention provides a method of operation of liquid extraction system for the isolation of the phytochemicals, comprising:
a) converting two solvents and CO2 together into vapor phase by plurality of pumps;
b) converting the vapor phase into a homogeneous gaseous mixture by a mixer chamber; and
c) sending the homogeneous gaseous mixture obtained at step (b) by a pump into a preheated heater;
wherein in the microwave oven the gaseous mixture comes in contact with a substance and extracts the phytochemicals from the given materials and finally isolated extracted collected into a collector.
In an embodiment, the present invention provides an advanced super critical liquid extraction system for the isolation of the phytochemicals. The system of the present invention uses two solvent chambers along with the CO2 chamber connected with the Pump which converted the solvent in to vapor phase and shifted the vapor of the solvent along with the CO2 vapor into the mixer where it converted it in to the homogeneous gaseous mixture.
In an embodiment, in the present invention an another pump located after the mixer shifted the homogeneous gaseous mixture in to the preheated heater where it converted the some remaining liquid component in to the gaseous component as well as homogeneous gaseous mixture will be charged and finally the homogeneous gaseous mixture of the two solvent and CO2 reaches in to the temperature programmed microwave oven which contain the material to be extracted. In the microwave oven the gaseous mixture come in contact with substance and extracted the phytochemicals from the given materials and finally isolated extracted collected into the collector.
There are various references for the currently available SFE technique such as off- flavoured compound and aroma eliminated from soybean oil by SFE. In this process SFE systems consisted of a CO2 tank, a compressor, a pressure gauge, a supercritical fluid pump, an extraction kettle (Xu et al. 2020). Alvarez et al, 2018. Extract the phytochemicals form soybean residue by the use of SFE. The SFE consists of CO2 tank, pump, extractor and collector. In present idea, the sample is completely mixed with two solvents and charged with the heater. As the heated sample progresses, it will be sent into an oven and solvent will break the cells of the sample with the higher efficiency.
, Claims:We Claim:
1. A liquid extraction system for the isolation of the phytochemicals, comprising:
a) at least two solvent chambers along with a CO2 chamber connected with a pump which converts the solvent into vapor phase;
b) a mixer chamber connected to the pump of the solvent chambers and the CO2 chambers where the pumps shift the vapor of the solvent along with the CO2 vapor into the mixer where it converted it into the homogeneous gaseous mixture;
c) an another pump mounted after the mixer chamber is configured to shift the homogeneous gaseous mixture into a preheated heater;
d) a microwave configured to receive homogeneous gaseous mixture which contain a material to be extracted,
wherein in the microwave oven the gaseous mixture comes in contact with a substance and extracts the phytochemicals from the given materials and finally isolated extracted collected into a collector.
2. The liquid extraction system for the isolation of the phytochemicals as claimed in claim 1, wherein the preheater is configured to converted remaining liquid component into the gaseous component.
3. The liquid extraction system for the isolation of the phytochemicals as claimed in claim 1, wherein the preheater is also configured to charge the homogeneous gaseous mixture.
4. The liquid extraction system for the isolation of the phytochemicals as claimed in claim 1, wherein the homogeneous gaseous mixture of the two solvent and CO2 reaches into the temperature microwave oven wherein the microwave oven is programmed for the extraction.
5. A method of operation liquid extraction system for the isolation of the phytochemicals as claimed in claim 1, comprising:
a) converting two solvents and CO2 together into vapor phase by plurality of pumps;
b) converting the vapor phase into a homogeneous gaseous mixture by a mixer chamber; and
c) sending the homogeneous gaseous mixture obtained at step (b) by a pump into a preheated heater;
wherein in the microwave oven the gaseous mixture comes in contact with a substance and extracts the phytochemicals from the given materials and finally isolated extracted collected into a collector.
Documents
Name | Date |
---|---|
202411090336-FORM-26 [25-11-2024(online)].pdf | 25/11/2024 |
202411090336-Proof of Right [25-11-2024(online)].pdf | 25/11/2024 |
202411090336-COMPLETE SPECIFICATION [21-11-2024(online)].pdf | 21/11/2024 |
202411090336-DECLARATION OF INVENTORSHIP (FORM 5) [21-11-2024(online)].pdf | 21/11/2024 |
202411090336-DRAWINGS [21-11-2024(online)].pdf | 21/11/2024 |
202411090336-EDUCATIONAL INSTITUTION(S) [21-11-2024(online)].pdf | 21/11/2024 |
202411090336-EVIDENCE FOR REGISTRATION UNDER SSI(FORM-28) [21-11-2024(online)].pdf | 21/11/2024 |
202411090336-FORM 1 [21-11-2024(online)].pdf | 21/11/2024 |
202411090336-FORM 18 [21-11-2024(online)].pdf | 21/11/2024 |
202411090336-FORM FOR SMALL ENTITY(FORM-28) [21-11-2024(online)].pdf | 21/11/2024 |
202411090336-FORM-8 [21-11-2024(online)].pdf | 21/11/2024 |
202411090336-FORM-9 [21-11-2024(online)].pdf | 21/11/2024 |
202411090336-REQUEST FOR EARLY PUBLICATION(FORM-9) [21-11-2024(online)].pdf | 21/11/2024 |
202411090336-REQUEST FOR EXAMINATION (FORM-18) [21-11-2024(online)].pdf | 21/11/2024 |
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