STEAM USE AND SAFETY SYSTEMS

Abstract

A solid oxide electrolyzer cell (SOEC) system including a stack of electrolyzer cells configured to receive water or steam in combination with hydrogen, and a steam recycle outlet configured to recycle a portion of the water or steam

Claims

1. A solid oxide electrolyzer cell (SOEC) system comprising: a stack of electrolyzer cells configured to receive water or steam in combination with hydrogen; and a steam recycle outlet configured to recycle a portion of the water or steam.

2. The SOEC of claim 1, wherein a hydrogen and steam exhaust stream is recycled back to the stack.

3. The SOEC system of claim 2, further comprising a splitter that supplies a portion of the hydrogen and steam exhaust to a steam recycle blower.

4. The SOEC system of claim 3, wherein a recycled portion of the hydrogen and steam exhaust includes steam and does not include hydrogen.

5. The SOEC system of claim 1, wherein the stack of electrolyzer cells is configured to cease receiving hydrogen when the SOEC system is operating at steady state.

6. The SOEC system of claim 1, wherein the stack of electrolyzer cells is configured to receive hydrogen when the SOEC system is in startup, shutdown, or when the SOEC system is not producing hydrogen.

7. The SOEC system of claim 1, wherein the stack of electrolyzer cells is configured to cease receiving hydrogen when the SOEC system detects a safety event.

8. The SOEC system of claim 7, wherein the safety event is detected by a pressure detector or a thermal detector.

9. The SOEC system of claim 1, wherein a combination of steam, hydrogen, and heated deionized water is supplied to a recycle steam inlet.

10. The SOEC system of claim 1, wherein steam output by the recycle steam outlet is mixed with hydrogen and a combination of steam and hydrogen is supplied to a recycle steam inlet.

11. The SOEC system of claim 1, wherein steam output by the recycle steam outlet is vaporized, mixed with hydrogen, and supplied to a recycle steam inlet.

12. The SOEC system of claim 1, wherein steam output by the recycle steam outlet is regulated by a water management system, mixed with hydrogen, and supplied to a recycle steam inlet.

13. A method of operating a solid oxide electrolyzer cell (SOEC) system comprising: receiving, at a stack of electrolyzer cells, water or steam in combination with hydrogen; and recycling, at a steam recycle outlet, a portion of the water or steam.

14. A solid oxide electrolyzer (SOEC) safety system comprising: a cabinet ventilator configured to provide ventilation to a cabinet and to ensure no buildup of flammable gas; a thermal detector having a thermal cutoff that is used inside the cabinet to shutoff the SOEC system in the event that the temperature exceeds the thermal cutoff; and a pressure detector including one or more pressure switches that are used on a hydrogen line to indicate both under pressure and over pressure events.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0009] The accompanying drawings, which are included to provide a further understanding of the invention and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and together with the description serve to explain the principles of the invention.

[0010] FIG. 1 is an SOEC system process flow diagram according to an example embodiment of the present invention.

[0011] FIG. 2 is an SOEC system process flow diagram according to another example embodiment of the present invention.

[0012] FIG. 3 is an SOEC system process flow diagram according to another example embodiment of the present invention.

[0013] FIG. 4 is an SOEC system process flow diagram according to another example embodiment of the present invention.

[0014] FIG. 5 is an SOEC system process flow diagram according to yet another example embodiment of the present invention.

DETAILED DESCRIPTION OF THE INVENTION

[0015] The various embodiments will be described in detail with reference to the accompanying drawings. Wherever possible, the same reference numbers will be used throughout the drawings to refer to the same or like parts. References made to particular examples and implementations are for illustrative purposes, and are not intended to limit the scope of the embodiments of the invention or the claims.

[0016] Values and ranges can be expressed herein as from “about” one particular value, and/or to “about” another particular value. When such a range is expressed, examples include from the one particular value and/or to the other particular value. Similarly, when values are expressed as approximations, by use of the antecedent “about” or “substantially” it will be understood that the particular value forms another aspect. In some embodiments, a value of “about X” may include values of +/- 1% X or +/- 5% X. It will be further understood that the endpoints of each of the ranges are significant both in relation to the other endpoint, and independently of the other endpoint. The values and ranges provide examples, but the embodiments of the invention are not so limited.

[0017] It will be apparent to those skilled in the art that various modifications and variations can be made to the present disclosure without departing from the spirit and scope of the disclosure. Since modifications combinations, sub-combinations and variations of the disclosed embodiments incorporating the spirit and substance of the disclosure may occur to persons skilled in the art, the disclosure should be construed to include everything within the scope of the appended claims and their equivalents.

[0018] In various embodiments of the present embodiments, steam is recycled in the SOEC system.

[0019] FIG. 1 is an SOEC system 100 according to an example embodiment of the present invention.

[0020] As illustrated in FIG. 1, SOEC system 100 includes air conduit 105, air blower 106, steam conduit 110, recycle steam inlet 111, recycle steam outlet 121, hotbox 150, optional hydrogen conduit 130, enriched air conduit 125, steam and hydrogen product outlet 120, splitter 160, and steam recycle blower 170.

[0021] According to an example configuration and operation, steam input at steam conduit 110 (e.g., supplying site or facility steam at varying pressures) can have a temperature of between about 100° C. and 110° C. (e.g., 105° C.) and a pressure of about 1 psig. In the various embodiments, steam may be input to the SOEC system 100 from an external source or may be generated locally. In some embodiments, multiple steam inlets may be configured to recive external and local steam, respectively. Alternatively, or additionally, water may be input to the SOEC system 100 and vaporized.

[0022] Air input (e.g., ambient air) at air conduit 105 may be ambient temperature, perhaps between about - 20° C. and + 45° C., at the local atmospheric pressure. Air from air conduit 105 is received at air blower 106, and air output by air blower 106 will be a slightly higher temperature than ambient due to the heat of compression. For example, the temperature of air output by air blower 106 may be about 30° C. at 1.0 psig as compared to 20° C. ambient air temperature.

[0023] Hydrogen from optional hydrogen conduit 130 may only be required for startup and transients when hydrogen is not being otherwise produced by SOEC system 100. For example, there is no longer a need for a separate hydrogen feed stream or hydrogen recycle steam at steady state. Pressure for this hydrogen stream is a design option determined at the time of site construction, and may be between about 5 psig and 3000 psig. The temperature is likely to be near ambient, as it is likely to be coming from storage.

[0024] Air input at air conduit 105, steam input at steam conduit 110, and hydrogen input at optional hydrogen conduit 130 are input to hotbox 150. In turn, hotbox 150 outputs steam and hydrogen product H.sub.2—H.sub.2O—G at steam and hydrogen product outlet 120 of hotbox 150, where G stands for Gross. Hotbox output H.sub.2—H.sub.2O—G may have a temperature between about 100° C. and 180° C. (e.g., 130° C.), a pressure of between about 0.1 and 0.5 psig.

[0025] In addition, hotbox output H.sub.2—H.sub.2O—G is input to splitter 160 and is split into a steam recycle stream RECH.sub.2OLP, where LP stands for low pressure, and a net product H.sub.2—H.sub.2O—N, where N stands for Net (e.g., output for commercial use or storage). Here, net product H.sub.2—H.sub.2ON may have a temperature between about 100° C. and 180° C. (e.g., 130° C.), a pressure of between about 0.1 psig and 0.5 psig. Steam recycle stream RECH.sub.2OLP may have a temperature of between about 100° C. and 180° C. (e.g., 130° C.), a pressure of between about 0.1 psig and 0.5 psig. Hotbox 150 may further output enriched air at enriched air conduit 125 that may have a temperature of between about 120° C. and 300° C., at essentially local atmospheric pressure (e.g., less than 0.5 psig or less than 0.05 psig).

[0026] Steam recycle stream RECH.sub.2OLP is input to steam recycle blower 170. The resulting recycled steam REC-STM may have a temperature of between about 100° C. and 180° C. (e.g., 140° C.), a pressure between about 0.5 and 1.5 psig (e.g., about 1 psig), and is input into hotbox 150 at recycle steam inlet 111. Additional steam or heat is supplied to recycle steam inlet 111 by steam recycle outlet 121, which captures air exhaust heat (e.g., ~280° C.) of hotbox 150. In some embodiments, there may be no recycled hydrogen feed included with the recycled steam.

[0027] As can be understood from FIG. 1, incoming steam temperature at steam conduit 110 (e.g., 105° C.) is low compared with a SOEC configuration with internal steam generation. A plurality of recycle loops can be configured to SOEC systems using both internal steam generation from recycle steam outlet 121 and external steam generation from steam conduit 110. In other words, recycle steam inlet 111 is configured to receive steam from steam conduit 110 and/or recycle steam outlet 121. Here, the embodiments optionally route the facility supplied steam from steam conduit 110, typically saturated and at a temperature of about 105° C., through the internal steam generation coils, one or more vaporizers, and/or other heating elements, and use the air exhaust heat (e.g., -280° C.) to further heat (i.e., superheat) the steam supply before the heat is released at enriched air conduit 125 through optional fan or enriched air blower 126.

[0028] Accordingly, in some embodiments there is approximately, 2-3kW of energy is available to preheat the steam at recycle steam outlet 121. As a result, the steam temperature into the hotbox is increased to between 140° C. and 160° C.

[0029] FIG. 2 is an SOEC system 200 process flow diagram according to another example embodiment of the present invention. The components of SOEC system 200 are similar to the components of SOEC system 100, as described in connection with FIG. 1, and the differences between systems 200 and 100 will now be described.

[0030] In the example embodiment, SOEC system 200 does not require use of input steam conduit 110 and recycle steam outlet 121. Instead, SOEC system 200 utilizes external steam 210 as well as heated deionized water conduit 205. Deionized water of deionized water conduit 205 can be heated by heater 206. Hydrogen is supplied by input hydrogen conduit 225. Each of external steam 210, input hydrogen conduit 225, and heated deionized water conduit 205 are supplied on the recycle loop downstream from steam recycle blower 170, as shown in FIG. 2. The resulting hydrogen and steam product is input at recycle steam inlet 111.

[0031] FIG. 3 is an SOEC system 300 process flow diagram according to another example embodiment of the present invention. The components of SOEC system 300 are similar to the components of SOEC system 100, as described in connection with FIG. 1, and the differences between systems 300 and 100 will now be described.

[0032] In the example embodiment, SOEC system 300 does not require use of input steam conduit 110 as well as the recycle loop by not utilizing splitter 160 and steam recycle blower 170, and their downstream. Instead, SOEC system 300 generates internal steam by heating deionized water of deionized water conduit 305 that is received at water inlet 310. Steam outlet by recycle steam outlet 121 is further heated by vaporizer 320 and mixed with hydrogen of input hydrogen conduit 325. The resulting hydrogen and steam product is input at recycle steam inlet 111, as shown in FIG. 3.

[0033] FIG. 4 is an SOEC system 400 process flow diagram according to another example embodiment of the present invention. The components of SOEC system 400 are similar to the components of SOEC system 100, as described in connection with FIG. 1, and the differences between systems 400 and 100 will now be described.

[0034] In the example embodiment, SOEC system 400 does not require use of input steam conduit 110 as well as the recycle loop by not utilizing splitter 160 and steam recycle blower 170, and their downstream. Instead, SOEC system 400 generates internal steam by heating deionized water of deionized water conduit 405 that is received at water inlet 410. Steam outlet by recycle steam outlet 121 is further heated by vaporizer 420 and mixed with hydrogen of input hydrogen conduit 425. In some configurations, a demister (not shown) is included at the output of vaporizer 420. In some configurations, excess steam can be vented to enriched air conduit 125. The resulting hydrogen and steam product is input at recycle steam inlet 111, as shown in FIG. 4.

[0035] FIG. 5 is an SOEC system 500 process flow diagram according to yet another example embodiment of the present invention. The components of SOEC system 500 are similar to the components of SOEC system 100, as described in connection with FIG. 1, and the differences between systems 500 and 100 will now be described.

[0036] In the example embodiment, SOEC system 500 does not require use of input steam conduit 110 as well as the recycle loop by not utilizing splitter 160 and steam recycle blower 170, and their downstream. Instead, SOEC system 500 generates internal steam by heating deionized water of deionized water conduit 505 that is received at water inlet 510. Steam outlet by recycle steam outlet 121 is regulated by water monitor system 520 (e.g., level transducer float type). Steam released and optionally heated and demisted by water monitoring system 520 is mixed with hydrogen of input hydrogen conduit 525. The resulting hydrogen and steam product is input at recycle steam inlet 111, as shown in FIG. 5.

[0037] In each of the various embodiments described herein, one or more detectors can be used to detect a safety event. For example, one or more pressure detectors and one or more thermal detectors can be used. One or more pressure detectors can be placed along input hydrogen conduits (e.g., 225, 325, 425, 525) to detect under pressure (e.g., under 5 PSI) and excess pressure (e.g., over 5 PSI). If a pressure detector is tripped, the system (i.e., hotbox 150) is shutdown. Additionally, one or more thermal detectors can be placed within the cabinet of the hotbox to detect excess heat (e.g., over 230° C.). Cabinet ventilation is provided and maintained by enriched air blower 126, for example. If a thermal detector is tripped, the system (i.e., hotbox 150) is shutdown.

[0038] The SOEC system (e.g., 100, 200, 300, 400, 500) cease receiving hydrogen when the SOEC system is operating at steady state or upon detection of a safety event. Additionally, the stack of electrolyzer cells in hotbox 150 can be configured to receive hydrogen when the SOEC system is in startup, shutdown, or when the SOEC system is not producing hydrogen or not producing enough hydrogen.

[0039] Accordingly, the various embodiments provide SOEC mechanical systems and associated safety systems. To operate an SOEC there are mechanical systems and components required to provide water, air, and start-up fuel. Safety systems also protect the system against fire and other damage to the surroundings and people in proximity. Operating the SOEC with required safety systems prevents harm and hazards due to leaking hydrogen and/or other failures. Other SOEC systems may include hazardous location devices, or double containment of fuel components.

[0040] It will be apparent to those skilled in the art that various modifications and variations can be made in the steam usage and safety systems of the present invention without departing from the spirit or scope of the invention. Thus, it is intended that the present invention cover the modifications and variations of this invention provided they come within the scope of the appended claims and their equivalents.