Fixed Tube Sheet Type Heat Exchanger

• Customization: Available
• Application: Cooler
• Principle: Mixing Heat Exchanger
• Model NO.: EXT-1000
• Style: Storage-Type
• Material: Stainless Steel
• Transport Package: Plywooden Case
• Specification: 1000 x 1000x 3000
• Trademark: Fly
• Origin: China
• HS Code: 8419500090
• Production Capacity: 50000tons

Product Description

Stainless Steel Floating Shell and Tube Heat Exchanger



Floating head heat exchanger is one of the most used heat exchanger. As shown in the name of it, in this design, one end of the tubesheet is fixed to the shell, while the other one can "float" freely inside the shell. Generally, both the shell and tube bundle are free of expansion, this permits no thermal stress is produced between shell and tube bundle, when the temperature difference of two medium is large. In addition, it is easy to inspect and clean mechanically the heat exchanger as the tube bundle can be removed absolutely. Floating head heat exchanger is widely used for the service where the temperature is high between the shell and tube bundle, or the dirty service, like the petroleum refinery.
With high reliability and wide adaptability, floating head heat exchanger has accumulated a wealth of experience during the long - term using process, and promoted its development constantly. So far, among all kinds of heat exchangers, floating head heat exchanger is still in a leading position.
Floating Head Heat Exchanger Design
According to different requirements, the floating head on a floating head heat exchanger can be designed into various types, in addition to consider that the tube bundle can move freely within the device, we must also take into the convenience of maintenance, installation, and cleaning for the heat exchanger.
Generally, there are four basic types of floating head heat exchanger - outside packed stuffing box (TEMA P), outside packed lantern ring (TEMA W), the floating head with backing device (TEMA S), and pull through (TEMA T) designs.
ANSON can manufacturer various kinds of floating head heat exchangers accordance with the TEMA, API660, and JISB8249. Other special requirements are also available.
Main technical parameters of Fixed tube sheet type heat exchanger
 

NORMINAL  DIAMETER	NORMINAL  PRESSURE	THE  PATH NO.OF TUBES	NO. OF  TUBES	NO. OF TUBES IN THE CENTER	FLOWING      AREA OF THE TUBE SECTION	CALCULATION OF HEAT TRANSFER AREA
DN	PN	N	n			m2
mm	Mpa				m2	L=1500mm	L=2000mm	L=3000mm	L=4500mm	L=6000mm	L=9000mm
159	1.60     2.50     4.00     6.40	1	15	5	0.0027	1.3	1.7	2.6	-	-	-
219			33	7	0.0058	2.8	3.7	5.7	-	-	-
273		1	65	9	0.0115	5.4	7.4	11.3	17.1	22.9	-
		2	56	8	0.0049	4.7	6.4	9.7	14.7	19.7	-
325		1	99	11	0.0175	8.3	11.2	17.1	26	34.9	-
		2	88	10	0.0078	7.4	10	15.2	23.1	31	-
		4	68	11	0.003	5.7	7.7	11.8	17.9	23.9	-
400	0.60      1.00       1.60      2.50       4.00	1	174	14	0.0307	14.5	19.7	30.1	45.7	61.3	-
		2	164	15	0.0145	13.7	18.6	28.4	43.1	57.8	-
		4	146	14	0.0065	12.2	16.6	25.3	38.3	51.4	-
450		1	237	17	0.0419	19.8	26.9	41	62.2	83.5	-
		2	220	16	0.0194	18.4	25	38.1	57.8	77.5	-
		4	200	16	0.0088	16.7	22.7	34.6	52.5	70.4	-
500		1	275	19	0.0486	-	31.2	47.6	72.2	96.8	-
		2	256	18	0.0226	-	29	44.3	67.2	90.2	-
		4	222	18	0.0098	-	25.2	38.4	58.3	78.2	-
600		1	430	22	0.076	-	48.8	74.4	112.9	151.4	-
		2	416	23	0.0368	-	47.2	72	109.3	146.5	-
		4	370	22	0.0163	-	42	64	97.2	130.3	-
		6	360	20	0.0106	-	40.8	62.3	94.5	126.8	-
700		1	607	27	0.1037	-	-	105.1	159.4	213.8	-
		2	574	27	0.0507	-	-	99.4	150.8	202.1	-
		4	542	27	0.0239	-	-	93.8	142.3	190.9	-
		6	518	24	0.0153	-	-	39.7	136	182.4	-
800	0.60       1.00      1.60      2.50      4.00	1	797	31	0.1408	-	-	138	209.3	280.7	-
		2	776	31	0.0686	-	-	134.3	203.8	273.3	-
		4	722	31	0.0319	-	-	125	189.8	254.3	-
		6	710	30	0.0209	-	-	122.9	186.5	250	-
900		1	1009	35	0.1783	-	-	174.7	265	355.3	536
		2	988	35	0.0873	-	-	171	259.5	347.9	524.9
		4	938	35	0.0414	-	-	162.4	246.4	330.3	498.3
		6	914	34	0.0269	-	-	158.2	240	321.9	485.6
1000		1	1267	39	0.2239	-	-	219.3	332.8	446.2	673.1
		2	1234	39	0.109	-	-	213.6	324.1	434.6	655.6
		4	1186	39	0.0524	-	-	205.3	311.5	417.7	630.1
		6	1148	38	0.0338	-	-	198.7	3.1	404.3	609.9
1100		1	1501	43	0.2652	-	-	-	394.2	528.6	797.4
		2	1470	43	0.1299	-	-	-	386.1	517.7	780.9
		4	1450	43	0.0641	-	-	-	380.8	510.6	770.3
		6	1380	42	0.0406	-	-	-	362.4	486	733.1
1200		1	1837	47	0.3246	-	-	-	482.5	646.9	975.9
		2	1816	47	0.1605	-	-	-	476.9	639.5	964.7
		4	1732	47	0.0765	-	-	-	454.9	610	920.1
		6	1716	46	0.0505	-	-	-	450.7	604.3	911.6
1300	0.25      0.60      1.00      1.60      2.50	1	2123	51	0.3752	-	-	-	557.6	747.7	1127.8
		2	2080	51	0.1838	-	-	-	546.3	732.5	1105
		4	2074	50	0.0916	-	-	-	544.7	730.4	1101.8
		6	2028	48	0.0597	-	-	-	532.6	714.2	1077.4

Main technical parameters of U type tube heat exchanger

NORMINAL DIAMETER	THE PATH NO. OF TUBES	NO. OF TUBES		NO. OF TUBES IN THE CENTER		FLOWING AREA OF THE TUBE SECTION(m2)			CALCULATION OF HEAT TRANSFER AREA  (m2)
DN	N	TUBE DIAMETER(mm)  d				d×δt			L=3000mm		L=6000mm
mm		19	25	19	25	19×2	25×2	25×2.5	19	25	19	25
325	2	38	13	11	6	0.0067	0.0045	0.0041	13.4	6	27	12.1
	4	30	12	5	5	0.0027	0.0021	0.0019	10.6	5.6	21.3	11.2
426	2	77	32	15	8	0.0136	0.0111	0.01	26.9	14.7	54.5	29.8
400	4	68	28	8	7	0.006	0.0048	0.0044	23.8	12.9	48.2	26.1
500	2	128	57	19	10	0.0227	0.0197	0.0179	44.6	26.1	90.5	53
	4	114	56	10	9	0.0101	0.0097	0.0088	39.7	25.7	80.5	52.1
600	2	199	94	23	13	0.0352	0.0326	0.0295	69.1	42.9	140.3	87.2
	4	184	90	12	11	0.0163	0.0155	0.0141	63.9	41.1	129.7	83.5
700	2	276	129	27	15	0.0492	0.0453	0.0411	-	-	194.1	119.4
	4	258	128	12	13	0.0228	0.0221	0.0201	-	-	181.4	118.4
800	2	367	182	31	17	0.065	0.063	0.0571	-	-	257.7	168
	4	346	176	16	15	0.0306	0.0304	0.0276	-	-	242.8	162.5
900	2	480	231	35	19	0.085	0.08	0.0725	-	-	336.2	212.8
	4	454	226	16	17	0.0402	0.0391	0.0355	-	-	317.8	208.2
1000	2	603	298	39	21	0.1067	0.1032	0.0936	-	-	421.5	273.9
	4	576	292	20	19	0.051	0.0505	0.0458	-	-	402.4	268.4
1100	2	738	363	43	24	0.1306	0.1257	0.114	-	-	514.6	332.9
	4	706	356	20	21	0.0625	0.0616	0.0559	-	-	492.2	326.5
1200	2	885	436	47	26	0.1566	0.151	0.1369	-	-	615.8	399
	4	852	428	24	21	0.0754	0.0741	0.0672	-	-	592.6