Erratum

This article refers to:

Progress of adsorption cycle and its hybrids with conventional multi-effect desalination processes

Progress of adsorption cycle and its hybrids with conventional multi-effect desalination processes.

K.C. Ng, K. Thu, M.W. Shahzad and W. Chun

IDA Journal of Desalination and Water Reuse. 6, 44–56.

DOI 10.1179/2051645214Y.0000000020.

Table 2 was incorrectly presented in the above paper. The table should have appeared as follows

Table 2. MED operation parameters at different heat source temperatures

MED Operation Parameters (3-effect MED)					Rate of primary energy input (kW_pe)	MED PR
Heating source temperature (°C )	T-SG (Vapor sat, °C )	T-S2 (vapor sat, °C )	T-S3 (vapor sat, °C )	MED water production (L/m^2.h)^1
38	37·4	37·2	37·0	1·5	2·10	2·92
40	38·7	38·4	38·1	2·0	2·91	2·74
42	40·5	40·0	39·8	2·5	3·80	2·63
44	42·3	41·8	41·5	2·9	4·73	2·50
46	44·0	43·4	43·0	3·4	5·90	2·35
48	45·7	45·0	44·5	3·9	7·27	2·19
50	47·4	46·7	46·2	4·5	8·69	2·12
55	52·3	51·5	50·5	5·9	10·91	2·20
60	57·1	55·4	54·4	6·8	11·92	2·33
65	62·0	60·0	58·6	7·4	12·45	2·43
70	66·8	63·9	62·8	7·9	12·93	2·49

Note: ¹Heat transfer area for evaporation in the 3-effect MED = 12 m², PR = performance ratio

The corrected article is available at: http://dx.doi.org/10.1179/2051645214Y.0000000020.