could you help me design a reactor? it is a continuous hydrogenation reaction.

please include catalyst particle size

reactor selection justification ( I am thinking fixed -bed catalytic reactor but feel free to select the approprate one)

reaction kinetics ( it would be helpfull if you can include data reference in case I decide to change any operations condition

rate law and new rate

selectivity is given

weigh of catalyst with detailed calculation and methods

step by step design equation

catalyst and reactor volume and dimension

pressure drop and its importance

space time

material of construction for different parts

I am design the reactor from the scratch from this source ""Improved processing stability in the hydrogenation of dimethyl maleate to -butyrolactone, 1,4-butanediol and tetrahydrofuran'' type it on google it will come up, but instead of dimethyl maleate the reaction starts from dimethyl succinate DMS) any thermal data or correlations might help as well. I have done the mass balance I guess the concentration, rate constant, -r could be calculated. (Coulson Richardson's V6 and levenspiel Chemical engineering books might help) Please! help!

	Mass Balance
	Material		input			output				Material		Molar mass	(g/mol)
		mol(kmol/hr)	Mass flow rate (kg/h)			Mass flow rate (kg/h)				SA		118.1
								x		H2O		18.02
	water	267.0366	4812		273.2519	4924				MeOH		32.05
	mthanol	162.8705	5220		370.2028	11865				DMS		146.16
	hydrgen	352.4752	712		0	0				H2O		2.02
	DMS	105.8019	15464		2.114122	309				GBL		86.1
	GBL	5.33101	459		36.43438	3137				BDO		90.14
	BDO	4.870202	439		71.22254	6420				THF		72.12
	THF				6.211869	448
	Total		27106			27103
			1 DMS + 2 H2 1 GBL + 2 MeOH
			1 GBL + 2 H2 1 BDO
			1 BDO1 THF + H2O
Operaing Conditions
Catalyst	CuZn			DMS conversion 98%
				GBL selection 30%
T	200			BDO selection 64%
P	50