Plant Layout 建厂方案
Technical Consultancy & Evaluation
技术支持和评估
Technical Consultancy & Evaluation
技术支持和评估
目录:
▶ EPS Plant Layout and Basic data
EPS泡沫厂布局和基本数据
▶ Complete EPS plant Reference Photos
完整的泡沫厂参考图片
▶ Machine Set Up
机器安装
▶ New Plant Survey
新建厂调查
▶ EPS Plant Layout and Basic data
EPS泡沫厂布局和基本数据
▶ Complete EPS plant Reference Photos
完整的泡沫厂参考图片
▶ Machine Set Up
机器安装
▶ New Plant Survey
新建厂调查
一、 EPS泡沫厂布局和基本数据
EPS泡沫厂基本数据
EPS泡沫厂规划 | 机台數目m/cs | 機台种別 | 成型面積 | 周 期 | 成型容積 / 立方米 | |
8 | Daisen 500C | 3.84 | 62 | 2.4 | ||
0 | FK810 EPS | 0 | 0 | 0 | ||
3 | FK813 EPS | 3.12 | 60 | 1.92 | ||
0 | FK1014 EPS | 0 | 0 | 0 | ||
0 | FK1018 EPS | 0 | 0 | 0 | ||
0 | FK1318 EPS | 0 | 0 | 0 | ||
3 | FK1214 EPS | 5.1 | 60 | 3.42 | ||
2 | Prefoamer | 0 | 0 | 0 | ||
Total amount machines : 机台總數目 | 16 | Amount | 12.06 | 52 | 7.74 | |
Total foam area As/m2 總成型面積 | 12.06 | table 1: simultaneity factor | ||||
cycle time tz/s 周期/秒 | 60 | number M/C | w | |||
cycles nz/h 總周期/小時 | 60 | 2 | 0.8 | |||
Simultaneity factor w acc. table 1 同步參數 | 0.5 | 4 | 0.75 | |||
6 | 0.7 | |||||
8 | 0.65 | |||||
Steam installation 蒸氣周邊 | 10 | 0.6 | ||||
11 | 0.5 | |||||
recommended flow rate up to 50 m length: cd in m/sec | 25 | |||||
special steam requirement mdspec. in kg/(m2z) | 5.6 | |||||
steaming time td in sec | 10 | |||||
limiting of peak demand ms in kg/sec | 3.38 | |||||
density pd9 of saturated steam with 9,0 bar | 5.15 |
density pd4 of saturated steam with 4,0 bar | 2.67 | |||||
density pd3 of saturated steam with 3,0 bar | 2.16 | |||||
volume flow Vsd in m3/s | 1.56 |
Steam boiler蒸氣鍋爐 | ||||||
steam requirement md of FTA in kg/h 蒸氣需求量 | 4052 | |||||
supply of boiler mft with 5% lossess in kg/h 蒸氣鍋爐供應量 | 4256 |
Steam accumulator 蒸氣儲能罐容積 | ||||||
when decreasing the pressure in the accumulator from 4 to 3 bar | ||||||
20 kg steam/m3 water are released, require accumulation volume | 3 |
Steam reducing valve 蒸氣減壓閥 | table 2: steam reducing valve | ||||
steam consumption mft in kg/h | 4265 | nom. width DN | kvs-value | ||
pressure proportion before and after red. valve p2/p1:4/9 bar | 0.44 | ||||
z-value | 91 | 15 | 3.2 | ||
m-value | 1 | 20 | 5 | ||
kv-value | 47 | 25 | 8 | ||
kvs-value | 59 | 32 | 12.5 | ||
steam reducing valve acc. table 2: nominal width 減壓閥口徑 | 80 | 40 | 20 | ||
50 | 32 | ||||
65 | 50 | ||||
Steam leads:蒸氣管道 | 80 | 80 | |||
between D-boiler and D-red. valve in mm | 108 | 100 | 125 | ||
between D-red. valve and D- accumulator in mm | 150 | 125 | 190 | ||
lead between D-accumulator and moulding machine in mm | 282 | 150 | 280 | ||
or a ring lead in mm | 199 | 200 | 420 | ||
250 | 500 |
Air installation 壓縮空氣周邊
High pressure network with 7 bar高壓壓縮空氣網絡7巴 | |||||
amount of machines for control air | 16 | ||||
number of fillers (17 fillers per m2 moulding area) | 205 | ||||
air consumption in l/sec per filler | 7 | ||||
filling time in sec. | 10 | ||||
air requirement 7bar in m3/h 高壓風每小時需求量 | 1149 | ||||
Supply of the compressor in m3/min壓縮風机每分鐘供應量 | |||||
with 5% losses | 20 | ||||
filling time /sec. | 10 | ||||
limiting of peak demand m3/sec. | 0.718 | ||||
pressure of lead / bar | 6 | ||||
lead diameter / mm 管道口徑 | 98 | ||||
as ring lead / mm | 69 | ||||
loading pressure of the air receiver / bar | 7 | ||||
unloading pressure of the air receiver / bar | 6 | ||||
volume of the air receiver / m3 壓縮風缸容量/立方米 | 4 |
High pressure network with 7 bar高壓壓縮空氣網絡7巴 | |||||
amount of machines for control air | 16 | ||||
number of fillers (17 fillers per m2 moulding area) | 205 | ||||
air consumption in l/sec per filler | 7 | ||||
filling time in sec. | 10 | ||||
air requirement 7bar in m3/h 高壓風每小時需求量 | 1149 | ||||
Supply of the compressor in m3/min壓縮風机每分鐘供應量 | |||||
with 5% losses | 20 | ||||
filling time /sec. | 10 | ||||
limiting of peak demand m3/sec. | 0.718 | ||||
pressure of lead / bar | 6 | ||||
lead diameter / mm 管道口徑 | 98 | ||||
as ring lead / mm | 69 | ||||
loading pressure of the air receiver / bar | 7 | ||||
unloading pressure of the air receiver / bar | 6 | ||||
volume of the air receiver / m3 壓縮風缸容量/立方米 | 4 |
Calculation of the reduction of energy能耗減省之計算 | |||||
Single Plant單一高壓網絡 | |||||
single plant with supply / m3/min 每分鐘需求量 | 42 | ||||
power of the plant in kW with 7 bar | 292 | ||||
lead diameter / mm 管道口徑 | 240 | ||||
volume of the air receiver / m3 壓縮風缸容量/立方米 | 12 | ||||
Double plant高低壓網絡 | |||||
power of the plant in kW with 7 bar | 141 | ||||
power of the plant in kW with 4 bar | 106 | ||||
amount of power / kW | 247 | ||||
Difference / KW | 45 | ||||
current costs / RMB/kwh | 1.2 | ||||
annual production hours | 4,800 | ||||
annual reduction /RMB 每年可減省 | 261,044 |
Water installation 冷水周邊
Mould cooling with 50 o C 模具冷水50度 | |||||
cooling time per cycle WZK / s. | 8 | ||||
hot water requirement (WZK) / m3/h 冷卻模具高溫水需求量 | 50.65 | ||||
limiting of peak demand / m3/s | 0.053 | ||||
hot water lead as stub cable / mm 管道口徑 | 150 | ||||
as ring lead / mm | 106 | ||||
number of pumps | 2 | ||||
average flow rate between 3 and 4 bar / m3/h | 20 | ||||
volume of water tank / m3 儲水缸之容積 | 1.0 | ||||
Condenser cooling with 25 0 C 冷凝水25度 | |||||
cooling time KK /s | 12 | ||||
average consumption / m2 foam area and cycle | 0.055 | ||||
number of vacuum pumps | 12 | ||||
requirement of cold water (KK) / m3/h 冷凝水需求量 | 45.20 | ||||
limiting of peak demand / m3/s | 0.029 | ||||
cold water lead as stub cable / mm 管道口徑 | 111 | ||||
as ring lead / mm | 79 | ||||
number of pumps | 2 | ||||
average flow rate between 3 and 4 bar / m3/h | 20 | ||||
volume of water tank / m3 儲水缸之容積 | 0.6 |
Single Plant單一網絡 | |||||
single plant with supply / m3/h 每小時需求量 | 95.9 | ||||
lead diameter / mm 管道口徑 | 183 | ||||
volume of the water tank / m3 儲水缸之容積 | 2.0 | ||||
Power of cooling tower: 冷水塔之能量 | |||||
hot water requirement (WZK) / m3/h 冷卻模具高溫水需求量 | 51 | ||||
cold water requirement (KK) / m3/h 冷凝水需求量 | 45 | ||||
amount of heat to be drawn off: /kcal/h | 1,355,940 | ||||
: /KJ/h | 5,677,050 | ||||
Condensate lead:冷凝水回收管道 | |||||
nominal width: /mm 管道口徑 | 273.7 |