You have successful laboratory results for suspension melt crystallization with an SSCC followed by a growth vessel and a wash column. For a pilot plant, you want to increase the feed flow rate by a factor of 100 while keeping the new and old growth vessels geometrically similar. Design to keep the particles suspended off the floor. What are values to use for the growth vessel in the pilot plant for \(\mathrm{D}_{\text {pilot-vessel }}, \mathrm{h}_{\text {pilot-vessel }}\), and \(\omega_{\text {pilot }}\) given as multiples of the laboratory values? What is the new power/volume ratio for the pilot plant growth vessel compared to the laboratory value?