{"id":1359,"date":"2024-10-08T14:09:12","date_gmt":"2024-10-08T14:09:12","guid":{"rendered":"https:\/\/www.hng-ua.com\/?page_id=1359"},"modified":"2024-11-21T13:47:55","modified_gmt":"2024-11-21T13:47:55","slug":"shell-and-tube-heat-exchangers","status":"publish","type":"page","link":"https:\/\/www.hng-ua.com\/en\/shell-and-tube-heat-exchangers\/","title":{"rendered":"Shell and tube heat exchangers"},"content":{"rendered":"\n

Heat-exchange equipment of own production:<\/h4>\n\n\n\n
\n
\"\"<\/figure>\n\n\n\n
\"\"<\/figure>\n<\/figure>\n\n\n

“KHIMMASHNEFTEGAZ” manufactures<\/strong> heat-exchange shell-and-tube apparatuses<\/strong> designed for heating and cooling of liquid and gaseous media in technological processes at enterprises of chemical, petrochemical, oil refining, gas industry, as well as for water heating in heating and hot water supply systems of residential, public and industrial buildings.
Our company manufactures all kinds of heat-exchange shell-and-tube apparatuses, both horizontal and vertical, according to the provided questionnaires or according to the Customer’s technical designs.<\/strong>
High quality and reliability of the manufactured equipment is ensured by:<\/p>\n

    \n
  • many years of production experience;<\/li>\n
  • cooperation with leading research institutes;<\/li>\n
  • maximum consideration of the customer’s interests and wishes.<\/li>\n<\/ul>\n

    Our company manufactures heat exchange equipment of various types:<\/strong><\/span><\/p>\n

    FLOATING HEAD SHELL-AND-TUBE HEAT EXCHANGERS <\/b><\/p>\n

    TU IN 29.2-00217432-012-2002<\/b><\/p>\n

    Designed for heating and cooling of liquid and gaseous media in technological processes of oil, chemical and gas industries.
    Shell and tube heat exchangers are multi-pass by tube space, vertical and horizontal by design. Material design depending on the applied media and operating parameters.
    Design, used materials, basic design characteristics and parameters meet world standards.<\/p>\n

    \"\u0410\u041f\u041f\u0410\u0420\u0410\u0422\u042b<\/p>\n

    Technical characteristics of heat exchangers:<\/p>\n

    \n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n
    Casing diameter, mm<\/td>\nPressure, Ru, MPa<\/td>\ndn, t\/o pipes<\/td>\nNumber of strokes<\/td>\nHeat exchange surface, m2<\/td>\nL,
    \u043c\u043c<\/td>\n    		H,
    \u043c\u043c<\/td>\n    		Dy,
    \u043c\u043c<\/td>\n    		Dy1, \u043c\u043c<\/td>\nA,
    \u043c\u043c<\/td>\n    		A1,
    \u043c\u043c<\/td>\n    		Weight, kg, not more<\/td>\n<\/tr>\n
    3000<\/td>\n6000<\/td>\n9000<\/td>\n<\/tr>\n
    325<\/td>\n <\/td>\n1,6; 2,5; 4,0<\/td>\n20<\/td>\n2<\/td>\n13<\/td>\n26<\/td>\n–<\/td>\n3960-6705<\/td>\n600<\/td>\n100<\/td>\n100<\/td>\n450<\/td>\n2350-5350<\/td>\n1550<\/td>\n<\/tr>\n
    25<\/td>\n10<\/td>\n20<\/td>\n–<\/td>\n1480<\/td>\n<\/tr>\n
    426<\/td>\n <\/td>\n1,6; 2,5;  4,0; 6,3<\/td>\n20<\/td>\n2<\/td>\n23<\/td>\n49<\/td>\n–<\/td>\n3690- 6750<\/td>\n714-810<\/td>\n100<\/td>\n100<\/td>\n500-550<\/td>\n2500-5250<\/td>\n2750<\/td>\n<\/tr>\n
    25<\/td>\n19<\/td>\n38<\/td>\n–<\/td>\n2650<\/td>\n<\/tr>\n
    530<\/td>\n <\/td>\n1,6; 2,5; 4,0; 6,3; 8,0<\/td>\n20<\/td>\n2<\/td>\n38<\/td>\n76<\/td>\n–<\/td>\n3835- 7400<\/td>\n954-1130<\/td>\n150<\/td>\n150<\/td>\n550-800<\/td>\n2200-5200<\/td>\n4430<\/td>\n<\/tr>\n
    25<\/td>\n31<\/td>\n62<\/td>\n–<\/td>\n4270<\/td>\n<\/tr>\n
    630<\/td>\n600<\/td>\n1,6; 2,5; 4,0; 6,3; 8,0<\/td>\n20<\/td>\n2
    4<\/td>\n    		–<\/td>\n117
    107<\/td>\n    		176
    160<\/td>\n    		6900- 10800<\/td>\n106-1300<\/td>\n200
    150<\/td>\n    		200<\/td>\n600-1000<\/td>\n5100-8100<\/td>\n6720<\/td>\n<\/tr>\n
    6700<\/td>\n<\/tr>\n
    25<\/td>\n2
    4<\/td>\n    		–<\/td>\n96
    86<\/td>\n    		144
    129<\/td>\n    		200
    150<\/td>\n    		200<\/td>\n6500<\/td>\n<\/tr>\n
    6480<\/td>\n<\/tr>\n
     <\/td>\n800<\/td>\n1,6; 2,5; 4,0; 6,3; 8,0<\/td>\n20<\/td>\n2
    4<\/td>\n    		–<\/td>\n212
    197<\/td>\n    		318
    295<\/td>\n    		7465- 11000<\/td>\n1060-1300<\/td>\n250
    200<\/td>\n    		250<\/td>\n700-1250<\/td>\n5100-7200<\/td>\n14250<\/td>\n<\/tr>\n
    14150<\/td>\n<\/tr>\n
    25<\/td>\n2
    4<\/td>\n    		–<\/td>\n170
    157<\/td>\n    		255
    235<\/td>\n    		250
    200<\/td>\n    		250<\/td>\n13850<\/td>\n<\/tr>\n
    13710<\/td>\n<\/tr>\n
     <\/td>\n1000<\/td>\n1,6; 2,5; 4,0; 6,3<\/td>\n20<\/td>\n2
    4<\/td>\n    		–<\/td>\n346
    330<\/td>\n    		519
    495<\/td>\n    		7615- 11250<\/td>\n1558-1860<\/td>\n300
    200<\/td>\n    		300<\/td>\n750-1330<\/td>\n5000-7200<\/td>\n23000<\/td>\n<\/tr>\n
    22850<\/td>\n<\/tr>\n
    25<\/td>\n2
    4<\/td>\n    		–<\/td>\n284
    267<\/td>\n    		426
    400<\/td>\n    		300
    200<\/td>\n    		300<\/td>\n23050<\/td>\n<\/tr>\n
    22800<\/td>\n<\/tr>\n
     <\/td>\n1200<\/td>\n1,6; 2,5; 4,0; 6,3<\/td>\n20<\/td>\n2
    4<\/td>\n    		–<\/td>\n514
    494<\/td>\n    		771
    741<\/td>\n    		7655- 11400<\/td>\n1780-1900<\/td>\n300
    250<\/td>\n    		300<\/td>\n820-1400<\/td>\n4760-7760<\/td>\n35500<\/td>\n<\/tr>\n
    35400<\/td>\n<\/tr>\n
    25<\/td>\n2
    4<\/td>\n    		–<\/td>\n426
    403<\/td>\n    		635
    604<\/td>\n    		300
    250<\/td>\n    		300<\/td>\n35500<\/td>\n<\/tr>\n
    35400<\/td>\n<\/tr>\n
     <\/td>\n1400<\/td>\n1,6; 2,5; 4,0<\/td>\n20<\/td>\n2
    4<\/td>\n    		–<\/td>\n715
    693<\/td>\n    		1072
    1040<\/td>\n    		7915- 11100<\/td>\n1980-2000<\/td>\n350
    250<\/td>\n    		350<\/td>\n1020-1270<\/td>\n4660-7660<\/td>\n34460<\/td>\n<\/tr>\n
    34450<\/td>\n<\/tr>\n
    25<\/td>\n2
    4<\/td>\n    		–<\/td>\n584
    561<\/td>\n    		876
    841<\/td>\n    		350
    250<\/td>\n    		350<\/td>\n35550<\/td>\n<\/tr>\n
    35500<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n

    SHELL AND TUBE HEAT EXCHANGERS WITH FIXED TUBE GRIDS AND A COMPENSATOR ON THE SHELL<\/b><\/span><\/p>\n

    \u0422\u0423 \u0423 00217432-012-2002<\/b><\/p>\n

    Designed for heating and cooling of liquid and gaseous media at temperatures of heat-exchanging media from minus 20 \u00b0\u0421 to plus 400 \u00b0\u0421 in technological processes of oil, chemical, petrochemical and gas industries.
    Conditional pressure 1,0 MPa (10 kgf\/cm2); 1,6 MPa (16 kgf\/cm2); 2,5 MPa (25 kgf\/cm2).
    Placement of holes for pipes in pipe grids and partitions by triangle vertices<\/p>\n

    \"\"<\/p>\n

    Technical characteristics of heat exchangers:<\/p>\n

    \n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n
    Casing diameter, mm<\/td>\nPressure, Ru, MPa<\/td>\ndn, t\/o pipes<\/td>\nNumber of strokes<\/td>\nHeat exchange surface, m2<\/td>\nL,
    \u043c\u043c<\/td>\n    		H,
    \u043c\u043c<\/td>\n    		Dy,
    \u043c\u043c<\/td>\n    		A,
    \u043c\u043c<\/td>\n    		A1,
    \u043c\u043c<\/td>\n    		Weight, kg, not more<\/td>\n<\/tr>\n
    1000<\/td>\n1500<\/td>\n2000<\/td>\n3000<\/td>\n4000<\/td>\n6000<\/td>\n9000<\/td>\n<\/tr>\n
    159<\/td>\n <\/td>\n1,6; 2,5<\/td>\n20<\/td>\n1<\/td>\n1<\/td>\n1,5<\/td>\n2,0<\/td>\n3,5<\/td>\n–<\/td>\n–<\/td>\n–<\/td>\n1400-3400<\/td>\n430<\/td>\n80<\/td>\n620-2620<\/td>\n–<\/td>\n265<\/td>\n<\/tr>\n
    25<\/td>\n–<\/td>\n–<\/td>\n2,0<\/td>\n3<\/td>\n–<\/td>\n–<\/td>\n–<\/td>\n<\/tr>\n
    273<\/td>\n <\/td>\n1,6; 2,5<\/td>\n20<\/td>\n1<\/td>\n4<\/td>\n6<\/td>\n8,5<\/td>\n12,5<\/td>\n–<\/td>\n–<\/td>\n–<\/td>\n1450-6450<\/td>\n544<\/td>\n100<\/td>\n600-2600<\/td>\n–<\/td>\n710<\/td>\n<\/tr>\n
    25<\/td>\n3<\/td>\n5,0<\/td>\n6,5<\/td>\n10,5<\/td>\n–<\/td>\n–<\/td>\n–<\/td>\n<\/tr>\n
    325<\/td>\n <\/td>\n1,6; 2,5<\/td>\n20
    25<\/td>\n    		1<\/td>\n–<\/td>\n9,5
    7,5<\/td>\n    		12,5
    10<\/td>\n    		19
    14,5<\/td>\n    		25
    19,5<\/td>\n    		–<\/td>\n–<\/td>\n2200-4700<\/td>\n596<\/td>\n100<\/td>\n570-2600<\/td>\n440<\/td>\n800<\/td>\n<\/tr>\n
    20
    25<\/td>\n    		2<\/td>\n–<\/td>\n8,5
    6,5<\/td>\n    		11
    9<\/td>\n    		17
    13<\/td>\n    		22,5
    17,5<\/td>\n    		–<\/td>\n–<\/td>\n2170-4670<\/td>\n745<\/td>\n<\/tr>\n
    426<\/td>\n400<\/td>\n1,0; 1,6; 2,5<\/td>\n20
    25<\/td>\n    		1<\/td>\n–<\/td>\n–<\/td>\n23
    17<\/td>\n    		34
    26<\/td>\n    		46
    35<\/td>\n    		68
    52<\/td>\n    		–<\/td>\n2790-6790<\/td>\n726<\/td>\n150<\/td>\n1520-5550<\/td>\n445; 460; 530<\/td>\n1850<\/td>\n<\/tr>\n
    20
    25<\/td>\n    		2<\/td>\n–<\/td>\n–<\/td>\n21
    16<\/td>\n    		31
    24<\/td>\n    		42
    31<\/td>\n    		63
    47<\/td>\n    		–<\/td>\n2720-6720<\/td>\n1940<\/td>\n<\/tr>\n
     <\/td>\n600<\/td>\n1,0; 1,6; 2,5<\/td>\n20
    25<\/td>\n    		1<\/td>\n–<\/td>\n–<\/td>\n51
    41<\/td>\n    		77
    62<\/td>\n    		102
    82<\/td>\n    		154
    124<\/td>\n    		–<\/td>\n2940-6840<\/td>\n1060<\/td>\n200<\/td>\n1450-5450<\/td>\n520; 545<\/td>\n3510
    3180<\/td>\n<\/tr>\n
    20
    25<\/td>\n    		2<\/td>\n–<\/td>\n–<\/td>\n48
    38<\/td>\n    		73
    58<\/td>\n    		97
    77<\/td>\n    		146
    116<\/td>\n    		–<\/td>\n2910-6910<\/td>\n3740<\/td>\n<\/tr>\n
    20
    25<\/td>\n    		4<\/td>\n–<\/td>\n–<\/td>\n44
    34<\/td>\n    		66
    51<\/td>\n    		88
    68<\/td>\n    		132
    101<\/td>\n    		–<\/td>\n<\/tr>\n
     <\/td>\n800<\/td>\n1,0; 1,6; 2,5<\/td>\n20
    25<\/td>\n    		1<\/td>\n–<\/td>\n–<\/td>\n92
    74<\/td>\n    		140
    112<\/td>\n    		186
    149<\/td>\n    		–<\/td>\n–<\/td>\n3140-7130<\/td>\n1254<\/td>\n250<\/td>\n1400-5450<\/td>\n630; 645; 650<\/td>\n6000-5420<\/td>\n<\/tr>\n
    20
    25<\/td>\n    		2<\/td>\n–<\/td>\n–<\/td>\n90
    71<\/td>\n    		135
    106<\/td>\n    		179
    142<\/td>\n    		–<\/td>\n–<\/td>\n3190-7190<\/td>\n6010<\/td>\n<\/tr>\n
    20
    25<\/td>\n    		4<\/td>\n–<\/td>\n–<\/td>\n83
    64<\/td>\n    		125
    97<\/td>\n    		169
    129<\/td>\n    		–<\/td>\n–<\/td>\n<\/tr>\n
     <\/td>\n1000<\/td>\n1,0; 1,6; 2,5<\/td>\n20
    25<\/td>\n    		1<\/td>\n–<\/td>\n–<\/td>\n–<\/td>\n220
    182<\/td>\n    		295
    244<\/td>\n    		444
    366<\/td>\n    		667
    551<\/td>\n    		4170-7320<\/td>\n1458<\/td>\n300<\/td>\n650<\/td>\n760<\/td>\n10870<\/td>\n<\/tr>\n
    20
    25<\/td>\n    		2<\/td>\n–<\/td>\n–<\/td>\n–<\/td>\n214
    175<\/td>\n    		286
    234<\/td>\n    		430
    353<\/td>\n    		648
    530<\/td>\n    		4260-7350<\/td>\n10830<\/td>\n<\/tr>\n
    20
    25<\/td>\n    		4<\/td>\n–<\/td>\n–<\/td>\n–<\/td>\n202
    163<\/td>\n    		270
    218<\/td>\n    		406
    329<\/td>\n    		610
    494<\/td>\n<\/tr>\n
    20
    25<\/td>\n    		6<\/td>\n–<\/td>\n–<\/td>\n–<\/td>\n203
    160<\/td>\n    		272
    214<\/td>\n    		409
    322<\/td>\n    		614
    486<\/td>\n<\/tr>\n
     <\/td>\n1200<\/td>\n1,0; 2,5<\/td>\n20
    25<\/td>\n    		1<\/td>\n–<\/td>\n–<\/td>\n–<\/td>\n–<\/td>\n426
    348<\/td>\n    		462
    525<\/td>\n    		949
    790<\/td>\n    		5300-7380<\/td>\n1662<\/td>\n350<\/td>\n3300-5300<\/td>\n785<\/td>\n13620<\/td>\n<\/tr>\n
    20
    25<\/td>\n    		2<\/td>\n–<\/td>\n–<\/td>\n–<\/td>\n–<\/td>\n415
    338<\/td>\n    		626
    509<\/td>\n    		949
    766<\/td>\n    		5430-10460<\/td>\n19660<\/td>\n<\/tr>\n
    20
    25<\/td>\n    		4<\/td>\n–<\/td>\n–<\/td>\n–<\/td>\n–<\/td>\n396
    318<\/td>\n    		596
    479<\/td>\n    		897
    722<\/td>\n<\/tr>\n
    20
    25<\/td>\n    		6<\/td>\n–<\/td>\n–<\/td>\n–<\/td>\n–<\/td>\n397
    316<\/td>\n    		597
    476<\/td>\n    		900
    716<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n

    SHELL AND TUBE HEAT EXCHANGERS<\/strong><\/span>
    WITH U-SHAPED TUBE BUNDLE<\/strong><\/span><\/p>\n

    Designed for heating and cooling of liquid and gaseous media in technological processes of chemical, petrochemical and gas industries.
    Temperature of heat-exchanging media from minus 30 \u00b0\u0421 to plus 400 \u00b0\u0421.
    Working environment – explosive, fire hazardous and environments belonging to 1-4 class of danger.
    The nominal pressure is 1,6 MPa (16 kgf\/cm2); 2,5 MPa (25 kgf\/cm2); 4,0 MPa (40 kgf\/cm2).<\/p>\n

    \"\"<\/p>\n

    Technical characteristics of heat exchangers:<\/p>\n

    \n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n
    Casing diameter, mm<\/td>\nPressure, Ru, MPa<\/td>\ndn, t\/o pipes<\/td>\nNumber of strokes<\/td>\nHeat exchange surface, m2<\/td>\nL,<\/span>
    \u043c\u043c<\/span><\/td>\n    		H,<\/span>
    \u043c\u043c<\/span><\/td>\n    		Dy,<\/span>
    \u043c\u043c<\/span><\/td>\n    		A,<\/span>
    \u043c\u043c<\/span><\/td>\n    		A1,<\/span>
    \u043c\u043c<\/span><\/td>\n    		Weight, kg, not more<\/td>\n<\/tr>\n
    3000<\/td>\n6000<\/td>\n9000<\/td>\n<\/tr>\n
    325<\/td>\n <\/td>\n2,5<\/td>\n20<\/td>\n2<\/td>\n13<\/td>\n26<\/td>\n–<\/td>\n3805-6550<\/td>\n600<\/td>\n100<\/td>\n450<\/td>\n2500; 5500<\/td>\n1250<\/td>\n<\/tr>\n
    25<\/td>\n10<\/td>\n20<\/td>\n–<\/td>\n<\/tr>\n
     <\/td>\n400<\/td>\n2,5<\/td>\n20<\/td>\n2<\/td>\n23<\/td>\n49<\/td>\n–<\/td>\n3940-6940<\/td>\n714<\/td>\n100<\/td>\n500<\/td>\n2500; 5500<\/td>\n2500<\/td>\n<\/tr>\n
    25<\/td>\n19<\/td>\n38<\/td>\n–<\/td>\n<\/tr>\n
     <\/td>\n500<\/td>\n2,5<\/td>\n20<\/td>\n2<\/td>\n43<\/td>\n85<\/td>\n–<\/td>\n4070-7100<\/td>\n954<\/td>\n150<\/td>\n550<\/td>\n2500; 5500<\/td>\n3700<\/td>\n<\/tr>\n
    25<\/td>\n34<\/td>\n66<\/td>\n–<\/td>\n<\/tr>\n
     <\/td>\n600<\/td>\n1,6;\u2116 2,5<\/td>\n20<\/td>\n2<\/td>\n–<\/td>\n120<\/td>\n178<\/td>\n7225-7290<\/td>\n1060<\/td>\n200<\/td>\n600<\/td>\n5400<\/td>\n5250<\/td>\n<\/tr>\n
    25<\/td>\n–<\/td>\n99<\/td>\n<\/tr>\n
     <\/td>\n800<\/td>\n1,6; 2,5; 4,0<\/td>\n20<\/td>\n2<\/td>\n–<\/td>\n224<\/td>\n331<\/td>\n7300-10550<\/td>\n1354<\/td>\n250<\/td>\n700<\/td>\n5400; 8400<\/td>\n12850<\/td>\n<\/tr>\n
    25<\/td>\n–<\/td>\n178<\/td>\n<\/tr>\n
     <\/td>\n1000<\/td>\n1,6; 2,5<\/td>\n20<\/td>\n2<\/td>\n–<\/td>\n383<\/td>\n565<\/td>\n7905-10960<\/td>\n1558<\/td>\n300<\/td>\n750<\/td>\n5500; 8500<\/td>\n17000<\/td>\n<\/tr>\n
    25<\/td>\n–<\/td>\n311<\/td>\n<\/tr>\n
     <\/td>\n1200<\/td>\n1,6; 2,5<\/td>\n20<\/td>\n2<\/td>\n–<\/td>\n564<\/td>\n831<\/td>\n8020-11100<\/td>\n1780<\/td>\n300<\/td>\n800
    850<\/td>\n    		5400; 8400<\/td>\n22200<\/td>\n<\/tr>\n
    25<\/td>\n–<\/td>\n471<\/td>\n<\/tr>\n
     <\/td>\n1400<\/td>\n1,6; 2,5<\/td>\n20<\/td>\n2<\/td>\n–<\/td>\n790<\/td>\n1160<\/td>\n8350-11865<\/td>\n1980<\/td>\n350<\/td>\n1000<\/td>\n5200; 8200<\/td>\n31000<\/td>\n<\/tr>\n
    25<\/td>\n–<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n

    TUBE BUNDLES FOR SHELL AND TUBE HEAT EXCHANGERS<\/strong><\/span><\/p>\n

    Tube bundles are designed for heating, cooling, condensation of liquid and gaseous media as part of heat exchangers with floating and fixed tube head used in technological processes of oil refining, chemical, petrochemical and gas industries.<\/span><\/p>\n

    Execution:<\/strong><\/p>\n

    Pipes – <\/b>brass, carbon steel (steel 10-20), heat-resistant steel (15\u04255\u041c), stainless steel (12\u042518\u041d10\u0422, 10\u042517\u041d13\u041c2\u0422). copper;
    <\/b>Pipe grids<\/strong> – carbon steel, bimetal (steel + brass), heat-resistant steel (15\u04255\u041c), stainless steel (12\u042518\u041d10\u0422, 10\u042517\u041d13\u041c2\u0422), copper.<\/p>\n

    Specifications:<\/strong><\/p>\n\n\n\n\n\n\n\n\n
    Significance<\/td>\nSize<\/td>\n<\/tr>\n
    Body diameter, mm<\/td>\n325 – 1800<\/td>\n<\/tr>\n
    Pressure, kgf\/cm2<\/td>\n16 – 83<\/td>\n<\/tr>\n
    Length of heat exchange tubes, mm<\/td>\n3000 – 1200<\/td>\n<\/tr>\n
    Diameter of heat exchanger pipes, mm<\/td>\n20; 25<\/td>\n<\/tr>\n
    Heat exchange surface,m2<\/td>\n9,4 – 2000<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n

    VAPORIZERS WITH VAPOR SPACE<\/strong><\/span><\/p>\n

    Designed for evaporation of gas fractions from liquid media, can be used as evaporators in chemical, petrochemical, oil refining and other industries.<\/p>\n

    \"\u0418\u0421\u041f\u0410\u0420\u0418\u0422\u0415\u041b\u0418<\/p>\n

    Specifications:<\/strong><\/p>\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n
    Inner diameter of the casing, mm<\/td>\n800; 1000<\/td>\n<\/tr>\n
    Nominal pressure, MPa (kgf\/cm\u00b2)<\/td>\n1,6(16); 2,5(25)<\/td>\n<\/tr>\n
    Temperature of heat-exchanging media, \u00b0\u0421<\/td>\nminus 30 \u0434\u043e +450<\/td>\n<\/tr>\n
    Range of heat exchanger tubes, mm<\/td>\n20; 25<\/td>\n<\/tr>\n
    Length of heat exchange tubes, mm<\/td>\n6000<\/td>\n<\/tr>\n
    Number of strokes through the tubes of the apparatus<\/td>\n2<\/td>\n<\/tr>\n
    Layout of heat exchanger tubes in tube grids<\/td>\non the vertices of the squares<\/td>\n<\/tr>\n
    Heat exchanger tubes spacing, mm<\/td>\n26; 32<\/td>\n<\/tr>\n
    Material execution<\/td>\n <\/td>\n<\/tr>\n
    of carbon steel grades<\/td>\n\u0441\u0442.3; steel 20; 09\u04132\u0421; 16\u0413\u0421<\/td>\n<\/tr>\n
    stainless steel grades<\/td>\n12\u042518\u041d10\u0422; 10\u042517\u041d13\u041c2\u0422<\/td>\n<\/tr>\n
    Design of heaters<\/td>\nWith U-tubes with floating head<\/td>\n<\/tr>\n
    Dimensions, mm<\/td>\n <\/td>\n<\/tr>\n
    for \u00d8800<\/td>\n8250 \u0445 1250<\/td>\n<\/tr>\n
    for \u00d81000<\/td>\n8250 \u0445 1400<\/td>\n<\/tr>\n
    Weight of the device not more than, kg<\/td>\n <\/td>\n<\/tr>\n
    for \u00d8800<\/td>\n4040<\/td>\n<\/tr>\n
    for \u00d81000<\/td>\n5050<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n

    WATER-VAPOR HEATER<\/strong><\/span><\/p>\n

    Designed for heating and hot water supply systems operating at 70\/150 \u00b0C, 70\/130 \u00b0C and 70\/95 \u00b0C. The heaters are two-way, four-way and with flat bottoms. Pipe bundles are produced on customer’s request.<\/p>\n

    \"\u041f\u041e\u0414\u041e\u0413\u0420\u0415\u0412\u0410\u0422\u0415\u041b\u042c<\/p>\n

    Specifications:<\/strong><\/p>\n\n\n\n\n\n
    Designation<\/td>\nHousing D, mm<\/td>\nL1 tubes, mm<\/td>\nL, \u043c\u043c<\/td>\nl, \u043c\u043c<\/td>\nl1, \u043c\u043c<\/td>\nDy, \u043c\u043c<\/td>\nDy1, \u043c\u043c<\/td>\nDy2, \u043c\u043c<\/td>\nF heating surface, m\u00b2<\/td>\nHeat production. Gcal\/h<\/td>\n<\/tr>\n
    \u041f\u041f1-9-7-II
    \u041f\u041f1-17-7-II
    \u041f\u041f1-24-7-II
    \u041f\u041f1-32-7-II
    \u041f\u041f1-53-7-II
    \u041f\u041f1-76-7-II
    \u041f\u041f1-108-7-II<\/td>\n    		325
    426
    480
    530
    630
    720
    820<\/td>\n    		3000<\/td>\n3590
    3630
    3750
    3790
    3915
    4015
    4155<\/td>\n    		2300
    2300
    2300
    2300
    2300
    2100
    2100<\/td>\n    		2000
    2000
    2000
    2000
    2000
    1900
    1900<\/td>\n    		100
    125
    150
    200
    200
    250
    300<\/td>\n    		100
    150
    150
    200
    250
    250
    300<\/td>\n    		50
    50
    50
    80
    80
    125
    125<\/td>\n    		9.5
    17.2
    24.4
    32.0
    53.9
    76.8
    108.0<\/td>\n    		1.13
    2.08
    2.94
    3.88
    6.55
    9.4
    13.3<\/td>\n<\/tr>\n
    \u041f\u041f1-6-2-II
    \u041f\u041f1-11-2-II
    \u041f\u041f1-16-2-II
    \u041f\u041f1-21-2-II
    \u041f\u041f1-35-2-II
    \u041f\u041f1-50-2-II
    \u041f\u041f1-71-2-II<\/td>\n    		325
    426
    480
    530
    630
    720
    820<\/td>\n    		2000<\/td>\n2590
    2630
    2750
    2800
    2915
    3015
    3155<\/td>\n    		1300
    1300
    1300
    1300
    1300
    1100
    1100<\/td>\n    		1100
    1100
    1100
    1100
    1100
    1000
    1000<\/td>\n    		100
    125
    150
    200
    200
    250
    300<\/td>\n    		100
    150
    150
    200
    250
    300
    300<\/td>\n    		50
    50
    50
    80
    80
    125
    125<\/td>\n    		6.3
    11.4
    16.0
    21.2
    35.3
    50.5
    71.0<\/td>\n    		0.585
    1.07
    1.52
    1.99
    3.38
    5.02
    6.84<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n

    HIGH-SPEED WATER-WATER HEATER<\/strong><\/span><\/p>\n

    Water-water high-speed sectional heaters for heating networks are designed for water heating in heating and hot water supply systems of residential, public and industrial buildings.<\/p>\n

    The heaters are made of smooth pipes of 57-325 mm diameter in lengths of 2 m and 4 m with carbon, stainless steel, brass tubes of 16, 20 and 25 mm diameter.<\/p>\n

    The heaters are sectional and are connected by means of gussets.<\/p>\n

    Maximum pressure is 1-1.6 MPa (10-16 kgf\/cm\u00b2) at water temperature up to 200 \u00b0C.<\/p>\n

    <\/p>\n

    \"\"<\/p>\n

    Specifications:<\/strong><\/p>\n

    \n\n\n\n\n
    Heater number<\/td>\nHousing D, mm<\/td>\nL, \u043c\u043c<\/td>\nF heating surface, mm\u00b2<\/td>\nL1, \u043c\u043c<\/td>\nl, \u043c\u043c<\/td>\nH, \u043c\u043c<\/td>\ndH, \u043c\u043c<\/td>\ndH1, \u043c\u043c<\/td>\nh, \u043c\u043c<\/td>\n<\/tr>\n
    1
    2
    3
    4
    5
    6
    7
    8
    9
    10
    11
    12
    13
    14
    15
    16<\/td>\n    		57
    57
    76
    76
    89
    89
    114
    114
    159
    159
    219
    219
    273
    273
    325
    325<\/td>\n    		2000
    4000
    2000
    4000
    2000
    4000
    2000
    4000
    2000
    4000
    2000
    4000
    2000
    4000
    2000
    4000<\/td>\n    		0.37- 28.0<\/td>\n2133
    4133
    2143
    4143
    2170
    4170
    2210
    4210
    2310
    4310
    2415
    4415
    2512
    4512
    2600
    4600<\/td>\n    		70
    70
    80
    80
    85
    85
    90
    90
    140
    140
    150
    150
    190
    190
    190
    190<\/td>\n    		200
    200
    200
    200
    240
    240
    300
    300
    400
    400
    500
    500
    600
    600
    600
    600<\/td>\n    		45
    45
    57
    57
    76
    76
    89
    89
    133
    133
    168
    168
    219
    219
    273
    273<\/td>\n    		45
    45
    57
    57
    76
    76
    89
    89
    114
    114
    168
    168
    219
    219
    219
    219<\/td>\n    		100
    100
    100
    100
    120
    120
    150
    150
    200
    200
    250
    250
    300
    300
    300
    300<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n

    END COOLERS XK-50, XK-100<\/strong><\/span><\/p>\n

    End coolers for stationary piston opposition compressors of general purpose with capacity of 50 m\u00b3\/min (\u0425\u041a-50), 100 m\u00b3\/min (\u0425\u041a-100) are designed for cooling of air directed to the consumer with simultaneous separation of moisture and oil from it.<\/p>\n

    Specifications:<\/strong><\/p>\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n
      <\/span><\/td>\n\u0425\u041a-50<\/span><\/td>\n\u0425\u041a-100<\/span><\/td>\n<\/tr>\n
    Working pressure, MPa (kgf\/cm\u00b2):<\/td>\n <\/span><\/td>\n <\/span><\/td>\n<\/tr>\n
    in the case<\/td>\n0,9(9)<\/span><\/td>\n0,9(9)<\/span><\/td>\n<\/tr>\n
    tubular<\/td>\n0,3(3)<\/span><\/td>\n0,3(3)<\/span><\/td>\n<\/tr>\n
    Air temperature, \u00b0\u0421:<\/td>\n <\/span><\/td>\n <\/span><\/td>\n<\/tr>\n
    at the entrance<\/td>\n160<\/span><\/td>\n160<\/span><\/td>\n<\/tr>\n
    at the output<\/td>\n60<\/span><\/td>\n60<\/span><\/td>\n<\/tr>\n
    Inlet water temperature, \u00b0C.<\/td>\n25<\/span><\/td>\n25<\/span><\/td>\n<\/tr>\n
    Heat exchange surface, m\u00b2<\/td>\n14<\/span><\/td>\n34<\/span><\/td>\n<\/tr>\n
    Diameter and wall thickness of the heat exchanger tube, mm<\/td>\n25 \u0445 2<\/span><\/td>\n25 \u0445 2<\/span><\/td>\n<\/tr>\n
    Capacity, m\u00b3:<\/td>\n <\/span><\/td>\n <\/span><\/td>\n<\/tr>\n
    hulls<\/td>\n0,515<\/span><\/td>\n0,925<\/span><\/td>\n<\/tr>\n
    pipe part<\/td>\n0,142<\/span><\/td>\n0,207<\/span><\/td>\n<\/tr>\n
    Material execution<\/td>\ncarbon steel<\/td>\ncarbon steel<\/td>\n<\/tr>\n
    Heat exchange surface, m\u00b2<\/td>\n3,9 – 93<\/span><\/td>\n0,55 – 4,6<\/span><\/td>\n<\/tr>\n
    Material execution<\/td>\ncarbon steel,
    stainless steel<\/td>\n    		carbon steel,
    stainless steel<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n

    TUBE-IN-TUBE HEAT EXCHANGERS<\/strong><\/span><\/p>\n

    Technical characteristics of heat exchangers:<\/strong><\/p>\n\n\n\n\n\n\n\n
    Type
    apparatus<\/td>\n    		Diameter , mm<\/td>\nLength of heat exchange pipes, m<\/td>\nCombination of conditional
    pressures
    inside
    and outside
    heat
    exchange
    pipes
    Rv \/ Rn , MPa<\/td>\n    		Heat exchange surface,
    \u043c2<\/td>\n    		Material execution<\/td>\n<\/tr>\n
    in the pipe space<\/td>\nno annular space<\/td>\n<\/tr>\n
    Single-flow GSTU 3-17-202-2000<\/td>\n133, 159, 219<\/span><\/td>\n89, 108, 133, 159<\/span><\/td>\n4,5; 6,0; 9,0<\/span><\/td>\n1,6\/1,6; 4,0\/1,6; 4,0\/4,0<\/span><\/td>\n5,0-18,0<\/span><\/td>\nCarbon steel Stainless steel<\/td>\n<\/tr>\n
    Multiflow GSTU 3-17-203-2000<\/td>\n89, 108<\/span><\/td>\n38, 48, 57<\/span><\/td>\n3,0; 4,5; 6,0; 9,0<\/span><\/td>\n1,6\/1,6; 1,6\/4,0; 4,0\/1 ,6; 4,0\/4,0<\/span><\/td>\n3,9-93,0<\/span><\/td>\n<\/tr>\n
    Single-flow GSTU 3-17-204-2000<\/td>\n57, 76, 89, 108<\/span><\/td>\n25, 38, 48, 57<\/span><\/td>\n1,5; 3,0; 4,5; 6,0;<\/span><\/td>\n\n

    6,3\/1,6; 6,3\/4,0; 10,0\/1,6; 10,0\/4,0 10,0\/6,3 16,0\/10,0<\/span><\/p>\n<\/td>\n

    		0,55-4,6<\/span><\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n\n\n

    “KHIMMASHNEFTEGAZ” will be glad to see you among our customers and partners.<\/strong><\/p>\n","protected":false},"excerpt":{"rendered":"

    Heat-exchange equipment of own production: “KHIMMASHNEFTEGAZ” manufactures heat-exchange shell-and-tube apparatuses designed for heating and cooling of liquid and gaseous media in technological processes at enterprises of chemical, petrochemical, oil refining, gas industry, as well as for water heating in heating and hot water supply systems of residential, public and industrial buildings.Our company manufactures all kinds […]<\/p>\n","protected":false},"author":1,"featured_media":0,"parent":0,"menu_order":0,"comment_status":"closed","ping_status":"closed","template":"","meta":[],"_links":{"self":[{"href":"https:\/\/www.hng-ua.com\/en\/wp-json\/wp\/v2\/pages\/1359"}],"collection":[{"href":"https:\/\/www.hng-ua.com\/en\/wp-json\/wp\/v2\/pages"}],"about":[{"href":"https:\/\/www.hng-ua.com\/en\/wp-json\/wp\/v2\/types\/page"}],"author":[{"embeddable":true,"href":"https:\/\/www.hng-ua.com\/en\/wp-json\/wp\/v2\/users\/1"}],"replies":[{"embeddable":true,"href":"https:\/\/www.hng-ua.com\/en\/wp-json\/wp\/v2\/comments?post=1359"}],"version-history":[{"count":3,"href":"https:\/\/www.hng-ua.com\/en\/wp-json\/wp\/v2\/pages\/1359\/revisions"}],"predecessor-version":[{"id":2146,"href":"https:\/\/www.hng-ua.com\/en\/wp-json\/wp\/v2\/pages\/1359\/revisions\/2146"}],"wp:attachment":[{"href":"https:\/\/www.hng-ua.com\/en\/wp-json\/wp\/v2\/media?parent=1359"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}