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US 7,484,425 B2 - Copyfluidenergyconversion.com/pdfs/Patent7484425.pdfUS 7,484,425 B2 FLUID FLOW METER WITH A BODY HAVING UPSTREAM AND DOWNSTREAM CONICAL PORTIONS AND AN INTERMEDIATE

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Page 1: US 7,484,425 B2 - Copyfluidenergyconversion.com/pdfs/Patent7484425.pdfUS 7,484,425 B2 FLUID FLOW METER WITH A BODY HAVING UPSTREAM AND DOWNSTREAM CONICAL PORTIONS AND AN INTERMEDIATE
Page 2: US 7,484,425 B2 - Copyfluidenergyconversion.com/pdfs/Patent7484425.pdfUS 7,484,425 B2 FLUID FLOW METER WITH A BODY HAVING UPSTREAM AND DOWNSTREAM CONICAL PORTIONS AND AN INTERMEDIATE
Page 3: US 7,484,425 B2 - Copyfluidenergyconversion.com/pdfs/Patent7484425.pdfUS 7,484,425 B2 FLUID FLOW METER WITH A BODY HAVING UPSTREAM AND DOWNSTREAM CONICAL PORTIONS AND AN INTERMEDIATE
Page 4: US 7,484,425 B2 - Copyfluidenergyconversion.com/pdfs/Patent7484425.pdfUS 7,484,425 B2 FLUID FLOW METER WITH A BODY HAVING UPSTREAM AND DOWNSTREAM CONICAL PORTIONS AND AN INTERMEDIATE
Page 5: US 7,484,425 B2 - Copyfluidenergyconversion.com/pdfs/Patent7484425.pdfUS 7,484,425 B2 FLUID FLOW METER WITH A BODY HAVING UPSTREAM AND DOWNSTREAM CONICAL PORTIONS AND AN INTERMEDIATE
Page 6: US 7,484,425 B2 - Copyfluidenergyconversion.com/pdfs/Patent7484425.pdfUS 7,484,425 B2 FLUID FLOW METER WITH A BODY HAVING UPSTREAM AND DOWNSTREAM CONICAL PORTIONS AND AN INTERMEDIATE
Page 7: US 7,484,425 B2 - Copyfluidenergyconversion.com/pdfs/Patent7484425.pdfUS 7,484,425 B2 FLUID FLOW METER WITH A BODY HAVING UPSTREAM AND DOWNSTREAM CONICAL PORTIONS AND AN INTERMEDIATE
Page 8: US 7,484,425 B2 - Copyfluidenergyconversion.com/pdfs/Patent7484425.pdfUS 7,484,425 B2 FLUID FLOW METER WITH A BODY HAVING UPSTREAM AND DOWNSTREAM CONICAL PORTIONS AND AN INTERMEDIATE
Page 9: US 7,484,425 B2 - Copyfluidenergyconversion.com/pdfs/Patent7484425.pdfUS 7,484,425 B2 FLUID FLOW METER WITH A BODY HAVING UPSTREAM AND DOWNSTREAM CONICAL PORTIONS AND AN INTERMEDIATE
Page 10: US 7,484,425 B2 - Copyfluidenergyconversion.com/pdfs/Patent7484425.pdfUS 7,484,425 B2 FLUID FLOW METER WITH A BODY HAVING UPSTREAM AND DOWNSTREAM CONICAL PORTIONS AND AN INTERMEDIATE
Page 11: US 7,484,425 B2 - Copyfluidenergyconversion.com/pdfs/Patent7484425.pdfUS 7,484,425 B2 FLUID FLOW METER WITH A BODY HAVING UPSTREAM AND DOWNSTREAM CONICAL PORTIONS AND AN INTERMEDIATE
Page 12: US 7,484,425 B2 - Copyfluidenergyconversion.com/pdfs/Patent7484425.pdfUS 7,484,425 B2 FLUID FLOW METER WITH A BODY HAVING UPSTREAM AND DOWNSTREAM CONICAL PORTIONS AND AN INTERMEDIATE
Page 13: US 7,484,425 B2 - Copyfluidenergyconversion.com/pdfs/Patent7484425.pdfUS 7,484,425 B2 FLUID FLOW METER WITH A BODY HAVING UPSTREAM AND DOWNSTREAM CONICAL PORTIONS AND AN INTERMEDIATE
Page 14: US 7,484,425 B2 - Copyfluidenergyconversion.com/pdfs/Patent7484425.pdfUS 7,484,425 B2 FLUID FLOW METER WITH A BODY HAVING UPSTREAM AND DOWNSTREAM CONICAL PORTIONS AND AN INTERMEDIATE

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