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What is a good method of minimizing shell side pressure drop in a shell and tube exchanger?

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Answer:

When shell pressure drop is critical and impingement protection is required, use rods or tube protectors in top rows instead of a plate. These create less pressure drop and better distribution than an impingement plate. An impengement plate causes an abrupt 90-degree turn of the shell stream, which causes extra pressure drop. Source: Gulley Computer Associates

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Is there a difference in MTD (Mean Temperature Difference) between "E" and "J" (Divided Flow) type shell and tube heat exchangers?Are there any alternatives to scraping a shell and tube if a capacity increase will make the pressure drop across the exchanger too large?