Delayed coking plant combined heating and power generation
A system includes a heat exchange system and a power generation system. The heat exchange system includes first, second, and third heat exchangers each operable as a continuous source of heat from a delayed coking plant. The first and second heat exchangers heat first and second fluid streams to produce heated first and second fluid streams, respectively. The heated second fluid stream has a lower temperature and a greater quantity of heat than the heated first fluid stream. The third heat exchanger heats a third fluid stream to produce a heated third fluid stream that includes the heated first fluid stream and a hot fluid stream. The heated third fluid stream has a lower temperature than the heated first fluid stream. The power generation system generates power using heat from the heated second and third fluid streams.
1. A system comprising:
a heat exchange system comprising:
a first heat exchanger configured to heat a first fluid stream with heat recovered from a first heat source in a delayed coking plant thereby producing a heated first fluid stream;
a second heat exchanger configured to heat a second fluid stream with heat recovered from a second heat source in the delayed coking plant thereby producing a heated second fluid stream, wherein the heated second fluid stream has a lower temperature and a greater quantity of heat than the heated first fluid stream;
a third heat exchanger configured to heat a plant stream in the delayed coking plant by exchange with a third fluid stream thereby producing a heated third fluid stream, wherein the third fluid stream includes the heated first fluid stream and a hot fluid stream; and
a power generation system configured to generate power using heat from the heated second fluid stream and the heated third fluid stream.
2. The system of claim 1 , further comprising a fluid storage tank configured to receive a fourth stream of hot fluid and to output the hot fluid stream.
3. The system of claim 2 , wherein the fourth stream is an intermittent stream and wherein the fluid storage tank is configured to pass the hot fluid stream continuously.
4. The system of claim 2 , further comprising a fourth heat exchanger configured to heat a fourth fluid stream from the delayed coking plant to produce the fourth stream of hot fluid.
5. The system of claim 4 , wherein the fourth hot stream has a greater quantity of heat and a lower temperature than the heated first fluid stream.
6. The system of claim 4 , wherein the fourth heat exchanger recovers heat from an output stream from a coker blowdown tower in the delayed coking plant.
7. The system of claim 4 , wherein the heat exchange system comprises multiple fourth heat exchangers each configured to heat a portion of the fourth fluid stream, wherein each fourth heat exchanger recovers heat from a corresponding intermittent heat source in the delayed coking plant.
8. The system of claim 1 , wherein the first heat exchanger recovers heat from a bottom stream from a debutanizer in the delayed coking plant.
9. The system of claim 1 , wherein the first heat exchanger recovers heat from a stream output from a fractionator in the delayed coking plant.
10. The system of claim 1 , wherein the heat exchange system comprises multiple first heat exchangers each configured to heat a portion of the first fluid stream, wherein each first heat exchanger recovers heat from a corresponding first heat source in the delayed coking plant.
11. The system of claim 1 , wherein the second heat exchanger recovers heat from an overhead stream from a fractionator in the delayed coking plant.
12. The system of claim 1 , wherein the second heat exchanger recovers heat from an inter-stage stream or a discharge stream of a coker gas compressor in the delayed coking plant.
13. The system of claim 1 , wherein the heat exchange system comprises multiple second heat exchangers each configured to heat a portion of the second fluid stream, wherein each second heat exchanger recovers heat from a corresponding second heat source in the delayed coking plant.
14. The system of claim 1 , wherein the temperature of the heated third fluid stream is less than the temperature of the third fluid stream.
15. The system of claim 1 , wherein the third heat exchanger is configured to heat a stripper bottom product from a stripper in the delayed coking plant by exchange with the third fluid stream.
16. The system of claim 1 , wherein the third heat exchanger is configured to heat a rich sponge oil stream from a sponge absorber in the delayed coking plant by exchange with the third fluid stream.
17. The system of claim 1 , wherein the heat exchange system comprises multiple third heat exchangers each configured to heat a corresponding stream in the delayed coking plant by exchange with a portion of the third fluid stream.
18. The system of claim 1 , wherein the power generation system comprises an Organic Rankine cycle system.
19. The system of claim 1 , wherein the system is integrated into the delayed coking plant as a retrofit to the delayed coking plant.