Economy And Capacity Test of a Three Ton York Ice Plant

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54. Range of temp., water, deg. 9.
55. B.T.U. per hr. in condensing water- --•• -- 51363.
56. Total heat removed from each lb. NH 3 , B.T.U.-- 583.3 57. Heat removed from NH3 per hr.
B.T.U. -41473.3 Freezing Tank 58. Range of Temp. Brine- - 2.37 59. B.T.U. per hr . from Brine 22586.
60. " " " to NH3 16 General Results 63. Tons of ice per ton of coal--- 1.775 64. » ■ " " I.H.P. steam .604 65. • " " " " KH 3 - .497 66. Mechanical Eff. of set -- 82.1,% 67. Actual coefficient of performance 3.15 68
.... Ideal " " " H.?
69. Efficiency of ref. process 26.9^& 70. Tonnage-- 1.88 HEAT EALAflCE A. - Heat received by cooling agent per hr .
1. Heat taken from brine 22586. B.T.U.
2. ■ e qui v. compressor r.H.P. — 7157. B.T.T .
3. Heat by radiation (by diff.) — 11670.3 B .T.TI.
41413.3 B.T.U.
B. - Heat given up by agent per hr.
1. Heat removed in condenser - - 41413.3 B.T.U.
CALCULATIONS 43. T.H.P. (Engine) - PLAN 33000 = 28 x 1/2 x 28 x 290 = 3.41 33000 44. Water Rate (Theoretical) Wr - 13750 W - 13750 .03806 — 18.8 "~ P 28 W = wt.


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