EP4724177A1 - System and method for utilizing transformer wasted energy with modular co2 capture systems - Google Patents

System and method for utilizing transformer wasted energy with modular co2 capture systems

Info

Publication number
EP4724177A1
EP4724177A1 EP24718077.1A EP24718077A EP4724177A1 EP 4724177 A1 EP4724177 A1 EP 4724177A1 EP 24718077 A EP24718077 A EP 24718077A EP 4724177 A1 EP4724177 A1 EP 4724177A1
Authority
EP
European Patent Office
Prior art keywords
heat
heat transfer
transformer
dac
wasted
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
EP24718077.1A
Other languages
German (de)
French (fr)
Inventor
Luiz CHEIM
Alan SBRAVATI
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Energy Ltd
Original Assignee
Hitachi Energy Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Energy Ltd filed Critical Hitachi Energy Ltd
Publication of EP4724177A1 publication Critical patent/EP4724177A1/en
Pending legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B01D53/0462—Temperature swing adsorption
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/50—Carbon oxides
    • B01D2257/504—Carbon dioxide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/06—Polluted air
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01F—MAGNETS; INDUCTANCES; TRANSFORMERS; SELECTION OF MATERIALS FOR THEIR MAGNETIC PROPERTIES
    • H01F27/00—Details of transformers or inductances, in general
    • H01F27/08—Cooling; Ventilating
    • H01F27/10—Liquid cooling
    • H01F27/12—Oil cooling
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00—Capture or disposal of greenhouse gases
    • Y02C20/40—Capture or disposal of greenhouse gases of CO2

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Treating Waste Gases (AREA)

Abstract

A system of using thermal energy in the form of wasted heat of a transformer to minimize required energy for CO2 Direct Air Capture (DAC) operation comprising a heat transfer unit configured to be coupled to a transformer and receiv wasted heat in the form of hot insulating liquid, and configured to be coupled to one or more CO2 DAC modules including CO2 adsorbent or absorbent medium to transfer wasted heat from the hot insulating liquid in the heat transfer unit to the one or more CO2 DAC modules where the transferred heat is used to heat the CO2 adsorbent or absorbent medium to minimize requid energy for CO2 DAC operation.

Description

SYSTEM AND METHOD FOR UTILIZING TRANSFORMER WASTED ENERGY WITH MODULAR CO2 CAPTURE SYSTEMS
TECHNICAL FIELD
[1] The embodiments described herein are generally directed to carbon dioxide (“CO2”) capturing heating systems and method.
BACKGROUND
[2] Examples of CO2 Direct Air Capture systems (DAC) for capturing carbon dioxide directly from air include fans which push air through a filter system that collects CO2. When the filter is saturated, CO2 is separated at high temperatures, which can then be used for variety of applications, such as growing vegetables, carbonating beverages, etc. CO2 DAC systems require a significant amount of energy to elevate capture unit temperature from ambient temperature, which may be around 20-40 degrees C to CO2 desorption temperature, which may be about 100-120 degrees C. This cyclic temperature variation is a very energy intensive process, often being a limitation for the economic viability of the application of the DAC technology.
SUMMARY
[3] An aspect of the disclosure involves a system of using thermal energy in the form of wasted heat of a transformer to minimize required energy for CO2 Direct Air Capture (DAC) operation comprising a heat transfer unit configured to be coupled to a transformer and receive wasted heat in the form of hot insulating liquid, and configured to be coupled to one or more CO2 DAC modules including CO2 absorbent medium to transfer wasted heat from the hot insulating liquid in the heat transfer unit to the one or more CO2 DAC modules where the transferred heat is used to heat the CO2 absorbent medium to minimize required energy for CO2 DAC operation.
[4] One or more implementations of the above aspect of the disclosure described immediately above comprises one or more of the following: an additional heating system configured to ensure that a second heat transfer liquid, which is independent of the hot insulating liquid from the transformer, is continuously at a required temperature for desorption of CO2 in the one or more CO2 DAC modules; the heat transfer unit is a heat exchanger; the additional heating system is a hot insulating liquid bath that the heat exchanger is disposed within, and the heat exchanger is configured to transfer heat from the hot insulating liquid to the second heat transfer liquid, and the hot insulating liquid bath is configured to ensure that the second heat transfer liquid is continuously at the required temperature for desorption of CO2 in the one or more CO2 DAC modules.
[5] Another aspect of the disclosure involves a method of using thermal energy in the form of wasted heat of a transformer to minimize required energy for CO2 Direct Air Capture (DAC) operation comprising receiving wasted heat in the form of hot insulating liquid from a transformer; transferring wasted heat from the hot insulating liquid in the heat transfer unit to one or more CO2 DAC modules where the transferred heat is used to heat CO2 absorbent medium in the one or more CO2 DAC modules to minimize required energy for CO2 DAC operation.
[6] One or more implementations of the above aspect of the disclosure described immediately above comprises one or more of the following: heating a second heat transfer liquid, which is independent of the hot insulating liquid from the transformer, with the hot insulating liquid from the transformer; and/or additionally heating the second heat transfer liquid to a required temperature for desorption of CO2 in the one or more CO2 DAC modules.
BRIEF DESCRIPTION OF THE DRAWINGS
[7] The details of the present disclosure, both as to its structure and operation, may be gleaned in part by study of the accompanying drawings, in which like reference numerals refer to like parts, and in which:
[8] FIG. 1 is a simplified schematic of an embodiment of a system of using thermal energy in the form of wasted heat of a transformer to minimize required energy for CO2 Direct Air Capture (DAC) operation.
[9] FIG. 2 is a schematic of an embodiment of a CO2 DAC module of FIG. 1;
[10] FIG. 3 is a more detailed schematic of the system of FIG. 1;
[11] FIG. 4 is a flow chart of an exemplary method of using thermal energy in the form of wasted heat of a transformer to minimize required energy for CO2 Direct Air Capture (DAC) operation. DETAILED DESCRIPTION
[12] With reference generally to FIGS. 1-3, an embodiment of a system 100 of using thermal energy in the form of wasted heat of a transformer 120 to minimize required energy for CO2 Direct Air Capture (DAC) operation or transformer wasted energy heat transfer system (“HTS”) will be described. The system 100 includes a heat transfer unit 125 configured to be coupled to the transformer 120 and receive wasted heat in the form of hot insulating liquid (e.g., mineral oil, natural ester, synthetic ester, silicone fluid, LFH (less flammable hydrocarbons), or bio-based hydrocarbons), and configured to be coupled to one or more CO2 DAC modules 130 including CO2 adsorbent or absorbent medium 140 to transfer wasted heat from the hot insulating liquid in the heat transfer unit 125 to the one or more CO2 DAC modules 130 where the transferred heat is used to heat the CO2 adsorbent or absorbent medium 140 for reducing the energy required to raise the material temperature to a desired setpoint temperature (e.g., 100-120 degrees C) for desorption of the CO2 from the CO2 adsorbent or absorbent medium 140. Although 100-120 degrees C is provided as an example of the desired setpoint temperature, the desired setpoint temperature may fluctuate with sorbent efficiency. An additional heating system 145 ensures that there is sufficient transferred heat to the CO2 adsorbent or absorbent medium 140 to raise the material temperature to the desired setpoint temperature.
[13] As illustrated in FIG. 2, the one or more CO2 DAC modules 130 may be industrial modules for CO2 removal that are self-contained and have the necessary equipment to perform the CO2 removal and storage. The CO2 DAC module(s) 130 include one or more fans 150 mounted to housing 160 to force air circulation through the CO2 adsorbent or absorbent medium 140 to separate CO2 from the ambient air. A CO2 DAC module heat exchanger 170 receives and uses the hot insulating liquid from the system 100 to heat up the CO2 adsorbent or absorbent medium 140 to the desired setpoint temperature for desorption of the CO2 from the CO2 adsorbent or absorbent medium 140. Flushed CO2 may be drawn out of the CO2 DAC module(s) 130 via a vacuum / filtration system 180, exit the CO2 DACs at exit 190, pass through one or more conduits 200 and delivered via a compressor 210 to/for a destination/application 220 (e.g., connecting to CO2 pipeline, underground injection, bottled transportation, local storage in tanks). The DAC modules hereby described is one example of DAC systems. It is not intended to limit the application of the present disclosure. [14] As illustrated in FIG. 3, the additional heating system 145 of the system 100 is a hot insulating liquid bath 230 and the heat transfer unit 125 is a hot insulating liquid bath heat exchanger 240 disposed in the hot insulating liquid bath 230. The system 100 further includes conduits 250 that couple ports 260, 270 of a hot insulating liquid manifold 280 to the heat exchanger 240, and conduits 290 that couple the hot insulating liquid bath 230 to the CO2 DAC module(s) 130 (e.g., at hot insulating liquid inlet 300, hot insulating liquid outlet 310). The hot insulating liquid manifold 280 may be part of a transformer cooling system 315. Wasted energy hot insulating liquid (e.g., at 80 - 90 degrees C) from the hot insulating liquid manifold 270 is transferred to the heat exchanger 240 to heat a second heat transfer liquid or an alternative heat transfer mechanism (“AHTM”), which is separate/independent from the hot insulating liquid from the hot insulating liquid manifold 270, in the hot insulating liquid bath 230 and returned to the hot insulating liquid manifold 280. The hot insulating liquid bath 230 heats the independent second heat transfer liquid or alternative heat transfer mechanism therein (e.g., to 100 - 120 degrees C), which is transferred from the hot insulating liquid bath 230 to the heat exchanger 170 of the CO2 DAC module(s) 130 via the conduits 290. The heat exchanger 170 transfers heat from the circulated second heat transfer liquid or alternative heat transfer mechanism from the hot insulating liquid bath 230 to the CO2 adsorbent or absorbent medium 140 to the desired setpoint temperature (e.g., about 100-120 degrees C) for CO2 desorption. Thus, the additional heating system 145 ensures that a second heat transfer liquid or alternative heat transfer mechanism, which is independent of the hot insulating liquid from the transformer 120, is continuously at a required temperature for desorption of CO2 in the one or more CO2 DACs.
[15] With reference to FIG. 4, a method 350 of using the transformer wasted energy heat transfer system 100 will now be described. In block 360, the system 100 receives (e.g., via the heat exchanger 240 disposed in the hot insulating liquid bath 230) wasted heat in the form of hot insulating liquid from the transformer 120 (e.g., via transformer cooling system 315). In optional block 370, if needed, the system 100 heats a second heat transfer liquid or alternative heat transfer mechanism (e.g., via the hot insulating liquid bath 230), which is independent of the hot insulating liquid from the transformer 120, with the hot insulating liquid from the transformer 120. In optional block 380, if needed, the system 100 additionally heats the second heat transfer liquid or alternative heat transfer mechanism to a required temperature for desorption of CO2 in the one or more CO2 DAC modules 130. In block 390, the system 100 transfers heat (e.g., via the heat transfer unit 125 and the second heat transfer liquid in the heat transfer liquid bath 230) to the heat exchanger 170 of the CO2 DAC module(s) 130 where the transferred heat is used to heat the CO2 adsorbent or absorbent medium 140 to minimize required energy for CO2 Direct Air Capture (DAC) operation. Alternative heat transfer mechanism(s)/technologies may also be used instead of the heat exchanger 170, still utilizing the wasted heat from the insulating liquid of a transformer.
[16] A main advantage of the system 100 and method 350 include the minimization of energy required to raise the CO2 DAC module temperature (e.g., to 100-120 degrees C, typically from ambient around 20 degrees C, a delta of at least about 80 degrees C) by utilizing the thermal energy that needs to be removed from transformer 120 for preventing its overheating as an input to raise the CO2 DAC module temperature. Assuming wasted hot insulating liquid from the transformer cooling system 315 is at about 80-90 degrees C, such delta in temperature (and consequently in required energy) would reduce drastically, thus making the entire system more efficient and utilizing transformer wasted energy to benefit the environment and companies to accrue carbon credits.
[1] The above description of the disclosed embodiments is provided to enable a person skilled in the art to make or use the invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the general principles described herein can be applied to other embodiments without departing from the spirit or scope of the invention. Thus, it is to be understood that the description and drawings presented herein represent a presently preferred embodiment of the invention and are therefore representative of the subject matter which is broadly contemplated by the present invention. It is further understood that the scope of the present invention fully encompasses other embodiments that may become obvious to those skilled in the art and that the scope of the present invention is accordingly not limited.
[2] Combinations, described herein, such as “at least one of A, B, or C,” “one or more of
A, B, or C,” “at least one of A, B, and C,” “one or more of A, B, and C,” and “A, B, C, or any combination thereof’ include any combination of A, B, and/or C, and may include multiples of A, multiples of B, or multiples of C. Specifically, combinations such as “at least one of A, B, or C,” “one or more of A, B, or C,” “at least one of A, B, and C,” “one or more of A, B, and C,” and “A,
B, C, or any combination thereof’ may be A only, B only, C only, A and B, A and C, B and C, or A and B and C, and any such combination may contain one or more members of its constituents A, B, and/or C. For example, a combination of A and B may comprise one A and multiple B’s, multiple A’s and one B, or multiple A’s and multiple B’s.

Claims

CLAIMS What is claimed is:
1. A system (100) of using thermal energy in the form of wasted heat of a transformer to minimize required energy for CO2 Direct Air Capture (DAC) operation, comprising: a heat transfer unit (125) configured to be coupled to a transformer (120) and receive wasted heat in the form of hot insulating liquid, and configured to be coupled to one or more CO2 DAC modules (130) including CO2 adsorbent medium (140) to transfer wasted heat from the hot insulating liquid in the heat transfer unit (125) to the one or more CO2 DAC modules (130) where the transferred heat is used to heat the CO2 adsorbent medium (140) to minimize required energy for CO2 DAC operation.
2. The transformer wasted energy heat transfer system (100) of claim 1, further comprising an additional heating system (145) configured to ensure that a second heat transfer liquid or alternative heat transfer mechanism, which is independent of the hot insulating liquid from the transformer (120), is continuously at a required temperature for desorption of CO2 in the one or more CO2 DAC modules (130).
3. The transformer wasted energy heat transfer system (100) of claim 2, wherein the heat transfer unit (125) is a heat exchanger (240).
4. The transformer wasted energy heat transfer system (100) of claim 3, wherein the additional heating system (145) is a heat transfer liquid bath (230) that the heat exchanger (240) is disposed within, and the heat exchanger (240) is configured to transfer heat from the hot insulating liquid to the second heat transfer liquid, and the heat transfer liquid bath (230) is configured to ensure that the second heat transfer liquid is continuously at the required temperature for desorption of CO2 in the one or more CO2 DAC modules.
5. A method of using thermal energy in the form of wasted heat of a transformer to minimize required energy for C02 Direct Air Capture (DAC) operation, comprising: receiving wasted heat in the form of hot insulating liquid from a transformer (120); transferring wasted heat from the hot insulating liquid in the heat transfer unit (125) to one or more CO2 DAC modules (130) where the transferred heat is used to heat CO2 adsorbent medium (140) in the one or more CO2 DAC modules (130) to minimize required energy for CO2 DAC operation.
6. The method of claim 5, further comprising heating a second heat transfer liquid or alternative heat transfer mechanism, which is independent of the hot insulating liquid from the transformer (120), with the hot insulating liquid from the transformer (120);
7. The method of claim 6, further comprising additionally heating the second heat transfer liquid or alternative heat transfer mechanism to a required temperature for desorption of CO2 in the one or more CO2 DAC modules (130).
EP24718077.1A 2023-06-06 2024-04-02 System and method for utilizing transformer wasted energy with modular co2 capture systems Pending EP4724177A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US202363471434P 2023-06-06 2023-06-06
PCT/EP2024/058903 WO2024251411A1 (en) 2023-06-06 2024-04-02 System and method for utilizing transformer wasted energy with modular co2 capture systems

Publications (1)

Publication Number Publication Date
EP4724177A1 true EP4724177A1 (en) 2026-04-15

Family

ID=90720377

Family Applications (1)

Application Number Title Priority Date Filing Date
EP24718077.1A Pending EP4724177A1 (en) 2023-06-06 2024-04-02 System and method for utilizing transformer wasted energy with modular co2 capture systems

Country Status (3)

Country Link
EP (1) EP4724177A1 (en)
CN (1) CN121443369A (en)
WO (1) WO2024251411A1 (en)

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103492046B (en) * 2011-01-20 2015-08-26 沙特阿拉伯石油公司 Used heat is used for CO 2car on reclaim and store reversible solid adsorption method and system
US11685658B2 (en) * 2020-03-30 2023-06-27 X Development Llc Producing carbon dioxide with waste heat
CA3186480A1 (en) * 2020-06-26 2021-12-30 Socpra Sciences Et Genie S.E.C. System and method for continuous gas adsorbate capture using adsorption/regeneration cycle
CN118139685A (en) * 2021-10-21 2024-06-04 国际壳牌研究有限公司 Systems and methods for maintaining continuous carbon dioxide capture

Also Published As

Publication number Publication date
CN121443369A (en) 2026-01-30
WO2024251411A1 (en) 2024-12-12

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