DESC0024981
Project Grant
Overview
Grant Description
Improved SIPH thermal particles for decarbonization of chemical production
Awardee
Grant Program (CFDA)
Awarding Agency
Funding Agency
Place of Performance
North Haven,
Connecticut
06473-3168
United States
Geographic Scope
Single Zip Code
Related Opportunity
Precision Combustion was awarded
Project Grant DESC0024981
worth $206,374
from the Office of Science in July 2024 with work to be completed primarily in North Haven Connecticut United States.
The grant
has a duration of 8 months and
was awarded through assistance program 81.049 Office of Science Financial Assistance Program.
The Project Grant was awarded through grant opportunity FY 2024 Phase I Release 2.
SBIR Details
Research Type
SBIR Phase I
Title
Improved SIPH Thermal Particles for Decarbonization of Chemical Production
Abstract
Decarbonization of industrial petrochemical manufacturing using thermal energy from Gen3 Concentrating Solar Power falling particle bed receiver technology will be demonstrated in this Phase I project. Meeting carbon and cost metrics will strongly support the goal of using Solar Industrial Process Heating to decarbonize industrial energy, especially in the difficult to decarbonize chemical manufacturing sector. using non-oxidative non-catalytic dehydrogenation of ethane to ethylene as a high-impact reaction that fits well with thermal energy supplied by CSP. Specifically, we will show greater than 85% decarbonization of ethylene production, as compared to commercial large volume ethane steam cracking, is achievable provided that proper selection of reactor design, operating conditions and improved thermal particle compositions are employed. Allowing for sales of hydrogen co-product and process steam or electric generation, and an approach using CSP thermal energy for all process power needs can achieve significant carbon-negative ethylene production while maintaining ethylene cost competitiveness. The Phase I project will focus on the key issues of thermal particle selection and reactor design to avoid operating in either carbon-forming or low ethylene yield modes and avoid particle degradation. Proposed work includes particle material selection and performance characterization, determining potential modifications to reaction kinetics in thermal particle beds, use of fluid and chemical process modeling to determine optimum reactor design and operating conditions, and analysis to demonstrate the cost and carbon impact benefits of the approach. Current processes for conversion of ethane, natural gas components, and petroleum fractions into petrochemical products involve extensive energy use, the same challenges facing commercial ethane or naphtha steam cracking. Using newer processes are not cost competitive with current petrochemical processes or face the same carbon-intensive endothermic energy needs. These issues can be overcome with the use of Gen3 Concentrating Solar Power thermal particles, which offer substantial cuts to carbon emissions while reducing capital costs, at energy costs comparable to or less than natural gas combustion. The simple particle-fluid reactor will have a scalable design that can be both economic to operate and be much smaller than conventional steam crackers. Success will significantly advance multiple energy goals, including those related to significant decarbonization and improved energy efficiency and independence, while also substantially broadening the applicable market for smaller scale and local ethylene production.
Topic Code
C58-17c
Solicitation Number
DE-FOA-0003202
Status
(Complete)
Last Modified 8/27/24
Period of Performance
7/22/24
Start Date
3/21/25
End Date
Funding Split
$206.4K
Federal Obligation
$0.0
Non-Federal Obligation
$206.4K
Total Obligated
Activity Timeline
Additional Detail
Award ID FAIN
DESC0024981
SAI Number
None
Award ID URI
SAI EXEMPT
Awardee Classifications
Small Business
Awarding Office
892430 SC CHICAGO SERVICE CENTER
Funding Office
892401 SCIENCE
Awardee UEI
KHBYLJYZAJP3
Awardee CAGE
0CZC4
Performance District
CT-03
Senators
Richard Blumenthal
Christopher Murphy
Christopher Murphy
Modified: 8/27/24