Water Cooling Plate Heat Exchanger

B (mm)	B1 (mm)	D (mm)	D1 (mm)	A (mm)	Volume (L)	area (m²)	weight (kg)	distributor	capacity (KW)
391.4	397.2	397.2	163.7	11+2.3n	0.16	0.11	6.5+0.42n	Q	60～200
391.4	397.2	397.2	163.7	11+2.2n	0.16	0.11	6.5+0.33n	Q	50～250
599	628	628	232	13+2.85n	0.4	0.21	13+0.82n	Q	150～450

Mold	clamp size	max width	max height	max length	interface size	max number of chip	max flow
BB30H	N(2.4+X)	180	490	680	32	90	13
BB60B	N(2.0+X)	320	930	1200	60	250	36
BB60H	N(3.0+X)	320	930	1200	60	203	36
BB65T	N(4.0+X)	410	700	1400	65	130	72
BB100B	N(3.95+X)	470	1069	1600	100	278	140
BB100H	N(3.95+X)	470	1069	1600	100	180	140
BB150B	N(2.5+X)	610	1815	3000	150	600	360
BB150T	N(3.95+X)	610	1815	3000	150	450	360
BB200T	N(2.5+X)	800	1435	2700	295	285	520
BB200H	N(4.0+X)	780	2150	3000	200	420	600
BB250B	N(2.5+X)	920	2900	3300	250	500	900
BB300B	N(3.5+X)	1100	2415	3360	300	300	997

 (1) Between the heat exchanger will produce the two-way medium mixing serious consequences occasions: ① corrosive and toxic occasions. Fluid tube side and shell side does not produce corrosive or toxic when not in contact with the phenomenon, but the tube, the shell of the two-phase fluid mixture may cause severe corrosion or poisoning. ② hazardous areas. When the tube, the shell of the two fluids are mixed (contact), it will cause fire and explosion. ③ equipment causing dirt occasions. When the tube, the shell of the two fluids are mixed, such as the formation of a resinous substance or polymer. ④ adverse chemical reaction of the occasion. In the tube, the shell of the two fluids after contact, so that a chemical reaction is limited or no response or adverse reactions, contamination of the product, the product quality.

     (2) tube, a big difference between the medium shell occasions. Add the design sheet in the cavity between the inner and outer tubes to a medium to reduce the tube shell between the pressure medium, which is the main purpose of using the double tube sheet structure type.