قرار مجلس الوزراء بشأن النظام الإماراتي للمركبات الهيدروجينية
Cabinet Resolution Regarding the UAE Regulation on Hydrogen-Fueled Vehicles System
النص الكامل
1
قرار مجلس الوزراء
لسنة2021
بشأن
النظام الإماراتي للمركبات الهيدروجينية
( قرار مجلس الوزراء رقم42) لسنة
2021
بشأن النظام الإماراتي للمركبات الهيدروجينية
:مجلس الوزراء
-
،بعد الاطلاع على الدستور
-
( وعلى القانون الاتحادي رقم1
) لسنة1972
،بشأن اختصاصات الوزارات وصلاحيات الوزراء، وتعديلاته
-
وعلى( القانون الاتحادي رقم21
) لسنة1995
،بشأن السير والمرور، وتعديلاته
-
( وعلى القانون الاتحادي رقم14
) لسنة2016
،بشأن المخالفات والجزاءات الإدارية في الحكومة الاتحادية
-
( وعلى القانون الاتحادي رقم10
) لسنة2018
،في شأن سلامة المنتجات
،وتعديلاته
-
وعلى( القانون الاتحادي رقم15
) لسنة2020
،في شأن حماية المستهلك
-
( وعلى المرسوم بقانون اتحادي رقم20
) لسنة2020
،بشأن المواصفات والمقاييس
-
( وعلى قرار مجلس الوزراء رقم35
) لسنة2015
بشأن
ال نظام
الإماراتي ل لرقابة على جهات
تقييم
،المطابقة
-
وعلى قرار مجلس( الوزراء رقم45
) لسننة2016
بشنأن مواصنفات قياسنية ةلزامية لدولة الإمارات العر ية
،المتحدة
-
( وعلى قرار مجلس الوزراء رقم30
) لسننة2017
في
شنأن تنظيم خدمات السنير والمرور والسنالمة المرورية ،
،وتعديلاته
-
و ناء
على ما عرضه وزير الصناعة والكنولوجيا المتقدمة، و،موافقة مجلس الوزراء
:قـــرّر
( المادة1)
التعريفات
في تطبيق أحكام هذا القرار، يقصد بالكلمات والعبارات التالية المعاني المبينة قرين كل منها، ما لم ِيقض سياق
النص
ب:غير ذلك
الدولة
:
.الإمارات العر ية المتحدة
الوزارة
:
وزارة الصناعة.والتكنولوجيا المتقدمة
الوزير
:
.وزير الصناعة والتكنولوجيا المتقدمة
الجهة المختصة
:
الجهة الحكومية الاتحادية أو المحلية في الدولة التي يقع ضننمن صننالحيتها تطبيق
.أي من أحكام هذا القرار
2
قرار مجلس الوزراء
لسنة2021
بشأن
النظام الإماراتي للمركبات الهيدروجينية
المنتج
: كنل مركبنة هيندروجينينة
ال يزيند وز هنا الإجمنا ي عن4536
،كيلوجرام و تشننننمنل
المركبة الخفيفة والحافلة الخفيفة والتي تزيد سننرعتها عن25
كم / سنناعة والتي
تستخدم الهيدروجين وقودا بديال من أجل القوة المحركة لتشغيلها.
المواصفة القياسية
:
وثيقنة تحندد صننننفنات السننننلعنة أو المنادة أو المنتج أو الخندمنة، أو كنل منا يخ ننننع
للقياس أو أوصننافها أو خصنناىصننها أو مسننتوي جود ها أو أبعادها ومقاييسننها أو
متطلبات السننالمة وافمان فكها، كما تشننمل المصننطرحات والرموز وطرق الاختبار
.وأخذ العينات والتغليف و طاقات البيان والعلامات
المواصننفة القياسننية
المعتمدة
:
المواصننفة القياسننية التي تعتمدها الوزارة، و شننار ةلكها بعبارة مواصننفة قياسننية
( لدولة الإمارات العر ية المتحدة ويرمز لها بن بالرمز (م ق/ ة ع م) أوUAE.S
.)
شهادة المطابقة
:
الشننننهنادة الصننننننادرة عن الوزارة، والتي ت كند مطنابقنة المنتج أو أي دفعنة مننه
.لمتطلبات المواصفة القياسية المعتمدة
شنننننهننادة المنطننابنقننة
الخليجية
:
شننننهنادة تصننننندرهنا جهنة مقبولنة بعند القينام بفحص الطراز وتقر بموج هنا بنأن
التصنميم الف ي للطراز الخاضنع للفحص يفي بمتطلبات اللواىف الفنية الخليجية
.الخاصة به
تقييم المطابقة
: أي نشنات دسنتخدم ب شنكل مباشنر أو رير مباشنر للتحقق من اسنتيفاء المنتج أو
.الخدمة للمتطلبات الفنية ذات العلاقة
جهة تقييم المطابقة
:
الجهننة المأننننجلننة أو المعتمنندة أو المقبولننة من الوزارة للقيننام بنن جراءات تقييم
المطنابقنة وفقنا للتشننننر عنات
الننافنذة في هنذا الشننننأن ، وتشننننمنل مخت رات الفحص
والمعنناير ة وجهننات التفتيا وجهننات اختبننار الجنندارة وجهننات منف الشننننهننادات
.للأنظمة أو اففراد أواملنتجات
سلسلة التزويد
:
،كافة المراحل التي يمر بها المنتج بدءا من الإنتاج افو ي حتى وصننوله ة ى المسننتهلك
بما في ذلك مراحل الاستيراد والتصنيع وتح ير المنتج ومعالجته وتعبئته وتغليفه
.وتجهيزه وطرحه
المزود
:
المُصنننُع أو المُعملِ ا أو المعالت أو المسنننتورد أو المخزن للمنتج أو أي موزع رىي ننن ي أو
فرعي أو أي شننخص يكون لنشنناطه أثر على خصنناىص المنتج، أو أي مم ل تجاري
أو قانوني يكون مس ولا عن استيراد المنتج.
( المادة2)
نطاق
التطبيق
تسري أحكام هذا القرار على كافة
المنتجات التي يتم طرحها
.في أسواق الدولة بما في ذلك المناطق الحرة
3
قرار مجلس الوزراء
لسنة2021
بشأن
النظام الإماراتي للمركبات الهيدروجينية
المادة(3)
مسؤوليات الجهات المختصة
تتو ى الجهات المختصة القيام بالآتي:
1.
التأكد من استيفاء
المنتج للشروت وافحكام الواردة بهذا القرار
قبل دخوله
وتأجيله في الدولة.
2.
القيام بمهام الرقابة على افسننننواق للتأكد من حصننننوو المنتج على شننننهادة المطابقة وفقا فحكام هذا
القرار.
3. توفير
.مراكز ومتطلبات الفحص الدوري للمنتج
4.
.التنسيق مع الوزارة لفرض أي متطلبات أو التزامات أخري على المزود
( المادة4)
التزامات
المزود
:يجب على المزود، في أي مرحلة من مراحل سلسلة التزويد اللاتزام بما يأتي
1.
عدم دخوو أي منتج
ة ى الدولة خاضنع فحكام هذا القرار قبل حصنوله على شنهادة المطابقة أو شنهادة
المطابقة الخليجية.
2.
التعناون مع الوزارة والجهنة المختصنننننة وتزويندهنا بكنافنة الوثناىق والبيناننات التي تطل هنا بمنا في ذلنك تقنارير
فحص المنتج المبينة بما يتوافق مع
المتطلبات الواردة في( المرحق رقم3
)
.المرفق بهذا القرار
3.
ضنمان اسنتيفاء
المنتج للمتطلبات المحددة في هذا القرار ولتعليمات الاسنتخد ام المحددة له طواو فترة
.استخدام المنتج
4.
تحقيق متطلبات
المنتج
بما في ذلك متطلبات أداء المنتج وملصقات البيانات المطلو ة ومعدات السلامة
ومتطلبات تخزين الم
نتج و( فقا للمرحق رقم3) المرفق بهذا القرار.
5. توفير
اشننننتراطنات و يناننات و
إ جراءات التعنامنل مع الحوادت التي تصننننينب
المنتج
( وفقنا للمرحق رقم3
)
المرفق بهذا القرار.
6.
ضننننمنان توفير البنينة التحتينة النداعمنة
للمنتج
بمنا في ذلنك الورف الفنينة، والكوادر الم هلنة، وافجهزة
والمعدات المستخدمة في( عمليات الصيانة وفقا للمرحق رقم3) المرفق بهذا القرار.
7.
توفير الاشنتراطات الفنية للأجهزة والمعدات المسنتخدمة في محطات تزويد
المنتج
بالهيدروجين المناسنب
وفقا للمواصفات
الواردة في المرح
ق (2) المرفق بهذا القرار.
8.
توفير الاشننننتراطنات الفنينة لعملينات الصننننيناننة والتبندينل وإعنادة التركينب للمكوننات الخناصنننننة بنظنام
الهيدروجين في الم نتج
بما في ذلك متطلبات السلامة وتأهيل الكوادر الفنية للتعامل مع هذه الم
نتجات.
9. يجب اتباع التعليمات والإجراءات الفنية المعموو بها في الدولة عند التخزين أو
النقل والتداوو أو عند
التخلص من النفايات المستهلكة أو التالفة ل مان حماية البيئة
.والحفاظ على السلامة العامة
4
قرار مجلس الوزراء
لسنة2021
بشأن
النظام الإماراتي للمركبات الهيدروجينية
( المادة5)
شهادة المطابقة
دشترت إل ،صدار شهادة المطابقة
ما يأتي :
1.
استيفاء المنتج لجميع متطلبات هذا القرار
بما في ذلك متطلبات المواصفات
القياسية المبينة في المرحق
( رقم1
( ) والمرحق رقم2
) والمتطلبات الفنية الواردة( في المرحق رقم3)
.، والمرفقة بهذا القرار
2. تقنديم الوثناىق والمخططنات
الواجنب ةرفناقهنا والتي ت بن مطنابقنة المنتج وفقنا ملنا تقرره متطلبنات هنذا
.القرار
3.
.فحص المنتج في مخت رات مأجلة ومعتمدة لدي الوزارة أو معترف بها أو مقبولة من الوزارة
( المادة6
)
إجراءات تقييم المطابقة
1. يجب على المزود التقدم لرحصوو على شهادة المطابقة للمنتج
، وذلك وفق المتطلبات الآتية:
أ.
تقديم طلب
تأجيل المنتج لدي الوزارة.
ب. صورة عن رخصة صناعية أو تجارية، سارية المفعوو في الدولة.
ج. توقيع ةقرار المطابقة حسب النموذج المعتمد من الوزارة.
د.
تقنديم كنافنة الوثناىق والبيناننات الخناصنننننة بناسننننتيفناء ومطنابقنة المنتج للمتطلبنات الفنينة
الواردة
في
( المرحق رقم3) المرفق بهذا القرار.
ه.
تحديد الخصاىص الا
سمية للمنتج والتي يجب تأجيلها على بطاقة البيان.
2.
تكون شهادة المطابقة الصادرة وفق أحكام هذا القرار سارية المفعوو ملدة سنة من تاريخ صدورها، وتجدد
بشكل سنوي في حاو استيفائها للشروت
ال اردة و في أحكام هذا ال.قرار
3.
يتحمل المصنع/المورد تكاليف أي فحص أو اختبار للمنتج تطلبه الوزارة خالو فترة مطابقة المنتج.
4.
في حاو حصنوو المنتج على شنهادة المطابقة الخليجية، فال يتطلب ذلك الحصنوو على شنهادة المطابقة من
الوزارة.
5.
يحق للوزارة القينام بزينارات مصنننننعينة، متى اقت ننننن الحناجنة لال
طالع على عملينات ا لتصنننننيع وح ننننور
الا ختبارات المطلو ة وفقا
للمواصفات القياسية
الواردة
( في المرحق رقم1) المرفق بهذا القرار.
( المادة7
)
الرقابة ومسح الأسواق
1.
،يخ ننع المنتج عند طرحه في افسننواق للرقابة وتتو ى الوزارة أو الجهة المختصننة، حسننب مقت نن ى الحاو
اتخاذ الإجراءات اللازمة ملراقبته للتأكد من اسنتمرارية مطابقته لشنهادة المطابقة في جميع مراحل سنلسنلة
التزويد، ولها في سبيل ذلك اتخاذ أي من الإجراءات الآتية:
5
قرار مجلس الوزراء
لسنة2021
بشأن
النظام الإماراتي للمركبات الهيدروجينية
أ.
،التأكد أن جميع منافذ طرح المنتج في الدولة ملتزمة بحظر اسنتيراده أو طرحه في افسنواق المحلية
ةال بعد حصوله على شهادة المط
ابقة.
ب.
سننننحنب عيننات من المنتج، من افسننننواق أو من مسننننتودعنات المزودين، وذلنك إلجراء الاختبنارات
اللازمة والتأكد من مدي مطابقتها لمتطلبات هذا القرار.
ج.
اتخناذ الإجراءات المنناسننننبنة في مواجهنة المنتجنات المخنالفنة فحكنام هنذا القرار، بمنا في ذلنك تعليق أو
ةلغاء شهادة.المطابقة للمنتجات المخالفة وسحب واستدعاء المنتجات رير المطابقة من السوق
د.
ةلزام المزود المس وو عن طرح المنتج المخالف، باستدعاىه وسحبه من افسواق المحلية، وتصويب
أوضنننناعه ةذا كان ذلك ممكنا أو ةلزامه ب عادته ة ى بلد المنشننننأ أو المصنننندر أو ةتالفه بما يتفق مع
التشننننر عنات المعموو بهنا بهنذا الشنننننأن، وذلنك ضننننمن المندة الزمنينة التي تحنددهنا الوزارة أو الجهنة
.المختصة، حسب مقت ى الحاو
ه. متابعة تنفﯿذ ا إلجر
اءات ا
ملشا
ر ة
لﯿها في هذه دة ملا ا.
2.
دعت ر المزود الذي تم أخذ العينة من المنتج الموجود لديه مسننن ولا عن عدم مطابقته لمتطلبات هذا القرار
ما لم ي ب رير ذلك، خالو الفترة التي تحددها الوزارة أو الجهة المختصة، حسب مقت ى الحاو.
( المادة8)
المخالفات والجزاءات
1.
دون الإخالو بأي عقو ة أو ةجراء ينص عليه
في أي تشننر ع نافذ في الدولة،
في حالة ارتكاب مخالفة في من
،أحكام هذا القرار لل
وزارة
أو الجهة المختصننة، حسننب مقت نن ى الحاو، توقيع جزاء أو أك ر من الجزاءات
الإدارية الآتية:
أ.
.التنسيق مع سلطة الترخيص إللغاء الرخصة التجارية للمزود المس وو عن المخالفة
ب. ةلغاء شهادة المطابقة الممنوحة للمنتج المخا.لف
ج.
تحميل المخالف نفقات وتكاليف ةزالة ومعالجة افضنننرار المترتبة على المخالفة في حاو عدم قيامه
.بالإزالة أو المعالجة
2.
في حاو عدم تمكن الوزارة ،أو الجهة المختصننننة، حسننننب مقت نننن ى الحاو من تحديد المسنننن وو عن عدم
مطابقة المنتج لمتطلبات هذا القرار فيعت ر الشنخص الذي تم ضنبة المخالفة لديه هو المسن وو عن عدم
.المطابقة ما لم ي ب عكس ذلك
المادة (9)
إجراءات التظلم
1.
( يجوز التظلم من القرارات الصادرة بمقت ى أحكام المادة8
) من هذا القرار، شريطة:اللاتزام بما يلي
6
قرار مجلس الوزراء
لسنة2021
بشأن
النظام الإماراتي للمركبات الهيدروجينية
أ. تقديم التظلم للوزير أو لرىيس الجهة المختصنننة
أو من يفوضننن مه و وفق الإجراءات التي تحدد
من
قبل الوزارة أو الجهة المختصننة، بحسننب مقت نن ى الحاو( ، وذلك خالو مدة ال تزيد على14
) يوم
.عمل من تاريخ تبليغ المخالف بالقرار الذي يررب بالتظلم منه
ب.
ةرفاق.الوثاىق اللازمة التي توضح سبب التظلم
2. يصنندر الوزير أو رىيس الجهة المختصننة
أو من يفوضنن و هم القرار الذي يراه مناسننبا بشننأن التظلم المقدم
( وفق أحكام هذه المادة خالو مدة ال تزيد على25
) يوم عمل من تاريخ تقديمه، ويكون القرار الصننادر بهذا
الشأن هاىيا ، و عت ر التظلم مرفوضا في حاو عدم اتخاذ أي ةجراء خالو المدة المحددة في هذا البند.
( المادة10
)
أحكام عامة
1.
تتو ى الوزارة
مسن ولية
تنفيذ أحكام هذا القرار ولها في سنبيل ذلك اتخاذ الإجراءات التي تراها مناسنبة
.لهذه الغاية، ويجوز لها تفويض بعض صالحيا ها لجهات تقييم المطابقة المقبولة
2.
تتو ى الوزارة مسنن ولية اسننتالم ودراسننة طلبات تأننجيل المنتج ومنحه شننهادات المطابقة وفق أحكام
هنذا القرار، ولهنا تفويض أي من الجهنات المختصننننننة أو تعيين جهنة تقييم مطنابقنة مقبولنة لتقييم
مطابقة المنتج، وفقا لقرار مجلس الوزراء بشأن النظام الإماراتي للرقابة على جهات تقييم.المطابقة
3.
يجب على المزود وافطراف ذات الصننلة التعاون التام مع الوزارة والجهات المختصننة وتقديم المعلومات
.ال رورية المطلو ة لتنفيذ أحكام هذا القرار
4.
( تعد المواصننفات القياسننية الواردة في المرحق رقم1
( ) والمرحق رقم2
) بهذا القرار مواصننفات قياسننية
ةلزامينة التطبيق فر راض تنفينذه، ولا يجوز طرح أي
منتج
منا لم
يكن مطنابق
أو مسننننتوفي فحكنام هنذا
.القرار
5.
يجوز للوزير تعديل أي من المواصنفات القياسنية أو المتطلبات الواردة في
المالحق المرفقة بهذا القرار
أو
اعتماد أي مواصنننفة قياسنننية أخري يتطل ها تنفيذ هذا القرار، وذلك وفقا للتشنننر عات النا فذة في هذا
الشأن.
( المادة11
)
أحكام انتقالية
يمنف المزود الذي طرح منتج في افسنننواق قبل نشنننر هذا القرار مدة ال تزيد على سنننة ميلادية واحدة من تاريخ
نشر هذا القرار في الجريدة الرسمية
.لتوفيق أوضاع ذلك المنتج وفق أحكام هذا القرار
المادة(
12
)
اللإغاءات
.يُلغى كل حكم يخالف أو يتعارض مع أحكام هذا القرار
7
قرار مجلس الوزراء
لسنة2021
بشأن
النظام الإماراتي للمركبات الهيدروجينية
( المادة13
)
نشر القرا ر و
العمل به
.يُنشر هذا القرار في الجريدة الرسمية، و ُعمل به من اليوم التا ي لتاريخ نشره
محمد بن راشد آل مكتوم
رئيس مجلس الوزراء
______________________
:صدر عنا
: بتاريخ 9
/ رمضان /
1442هـ
: الموافق21
/أبريل /
2021م
8
قرار مجلس الوزراء
لسنة2021
بشأن
النظام الإماراتي للمركبات الهيدروجينية
( الملحق رقم1
) بشأن المواصفات القياسية الخاصة بالمركبات
المرفق
ب( قرار مجلس الوزراء رقم42) لسنة
2021
بشأن النظام الإماراتي للمركبات الهيدروجينية
No.
Standard No.
Standards Title
1
UAE.S GSO 36
Motor Vehicles - Methods of Test for Impact Strength - Part 1: Frontal Impact
2
UAE.S GSO 37
Motor Vehicles - Methods of Test for Impact Strength - Part 2: Rear Impact
3
UAE.S GSO 38
Motor Vehicles - Methods of Test for Impact Strength - Part 3A: Side Impact
4
UAE.S GSO 39
Motor Vehicles - Methods of Test for Impact Strength - Part 4: Roof Strength
5
UAE.S GSO 40
Motor Vehicles - Impact Strength
6
UAE.S GSO 41
Motor Vehicles: Front and Rear Exterior Protection Devices for Passenger Cars
(Bumpers etc.) and its Methods of Test
7
UAE.S GSO 42
Motor Vehicles: General Requirements
8
UAE.S GSO 48
Motor Vehicles: Conformity Certificates
9
UAE.S GSO 51
Passenger Car Tyres - Part 1: Nomenclature, Designation, Dimensions, Load
Capacities and Inflation Pressures
10
UAE.S GSO 52
Passenger Car Tyres - Part 2: General Requirements
11
UAE.S GSO 53
Passenger Car Tyres - Part 3: Methods of Test
12
UAE.S GSO 96
Motor Vehicles - Methods of Testing of Safety Belt
13
UAE.S GSO 97
Motor Vehicles - Safety Belts
14
UAE.S GSO 98
Motor Vehicles - Flammability of Interior Materials and Testing Methods
15
UAE.S GSO 99
Road Vehicles - Sound Signaling Devices – Technical Specifications
16
UAE.S GSO 279**
Car Upholstery - Testing Methods of Fabric for Car Seats
17
UAE.S GSO 280**
Car Upholstery - Fabric for Car Seats
18
UAE.S GSO 289**
Road Vehicles - Retro Reflective Number Plates and its Methods of Test
19
UAE.S GSO 290
Instruction Manual for Appliances Instruments and Equipment
20
UAE.S GSO 419
Motor Vehicles - Methods of Testing for Door Locks and Door Hinges
21
UAE.S GSO 420
Motor Vehicles - Door Locks and Door Hinges
22
UAE.S GSO 421
Motor Vehicles - Methods of Testing of Rear-view Mirrors
23
UAE.S GSO 422
Motor Vehicles – Rear-view Mirrors
24
UAE.S GSO 645
Multi-Purpose Vehicles, Trucks, Buses and Trailers Tyres - Part 1:
Nomenclature, Designation, Dimensions, Load Capacities and Inflation
Pressures
9
قرار مجلس الوزراء
لسنة2021
بشأن
النظام الإماراتي للمركبات الهيدروجينية
25
UAE.S GSO 646
Multi-Purpose Vehicles, Trucks, Buses and Trailers Tyres: Part 2: Method of
Test
26
UAE.S GSO 647
Multi-Purpose Vehicles, Trucks, Buses and Trailers Tyres: Part 3: General
Requirements
27
UAE.S GSO 971**
Motor Vehicles - Periodic Technical Inspection Manual
28
UAE.S GSO 1052 *
Motor Vehicles Tyres - Temporary Use Spare Wheel/Tyres and Their Methods
of Test
29
UAE.S GSO 1053
Motor Vehicles - Protection Against Theft
30
UAE.S GSO 1503
Motor Vehicle - Head Lamps Safety Requirements.
31
UAE.S GSO 1598
Motor Vehicles - Head Restraints and Their Methods of Test
32
UAE.S GSO 1625 *
Motor Vehicles - Speed Limiters - Part 2: Technical Requirements
33
UAE.S GSO 1626 *
Motor Vehicles - Speed Limiters - Part 3: Methods of Test
34
UAE.S GSO 1677
Motor Vehicles – Laminated Safety Glass
35
UAE.S GSO 1707
Motor Vehicles - Methods of Test for Impact Strength - Part 3B: Moving Barrier
Side Impact (In accordance to US standards)
36
UAE.S GSO 1708
Motor Vehicles - Methods of Test For Impact Strength - Part 3C: Moving Barrier
Side Impact (In accordance to European standards)
37
UAE.S GSO 1709 *
Motor Vehicles – Child Restraint Systems
38
UAE.S GSO 1710 *
Motor Vehicles – Methods of Testing of Child Restraint
39
UAE.S GSO 1711 *
Motor vehicles – Speed Limiters - Part 1: General requirements, Equipment
Inspection, Certification and type approval
40
UAE.S GSO 1780
Motor Vehicles – Vehicle Identification Number (VIN) - Requirements
41
UAE.S GSO 1781
Motor Vehicles - World Manufacturer Identifier
42
UAE.S GSO 1782
Motor Vehicles – Vehicle Identification Number (VIN) – Location and
attachment
43
UAE.S GSO 1783
Passenger Car Tyres - Tread wear, Traction and Temperature- Resistance
Grading
44
UAE.S GSO 1784
Passenger Car Tyres - Method of Testing of Tyre Temperature Resistance
Grading
45
UAE.S GSO ISO 3537
Motor Vehicles - Safety Glazing Materials - Mechanical Tests
46
UAE.S GSO ISO 3538
Road Vehicles - Safety Glasses - Test Methods for Optical Properties.
47
UAE.S GSO ISO
6311**
Motor Vehicles –Methods of Testing Brake Linings – Part 1: Internal Shear
Strength of Lining Material.
48
GSO-ECE- 13H
Motor Vehicles: Braking System of Passenger Cars and Multi-Purpose Vehicles
10
قرار مجلس الوزراء
لسنة2021
بشأن
النظام الإماراتي للمركبات الهيدروجينية
49
GSO-ECE- 13H-1
Motor Vehicles: Methods of Test for Braking System – Part 1: Braking
Performance
50
GSO-ECE- 13H-2
Motor Vehicles: Methods of Test for Braking System – Part 2: Determination
of Capacity of Energy Storage Devices
51
GSO-ECE- 13H-3
Motor Vehicles: Methods of Test for Braking System – Part 3: Determination
of Distribution of Braking among the Axles of Vehicles
52
GSO-ECE-13H-4
Motor Vehicles: Methods of Test for Braking System – Part 4: Determination
of Function of Anti-Lock Systems
53
GSO-ECE-13H-5
Motor Vehicles: Methods of Test for Braking System – Part 5: Determination
of Performance of Brake Lining Using Inertia Dynamometer
54
GSO-ECE-13H-6
Motor Vehicles: Methods of Test for Braking System – Part 6: Determination
of Coefficient of Adhesion
*
**
Applicable for certification if provided or the vehicle is designed for.
Not applicable for Certification.
11
قرار مجلس الوزراء
لسنة2021
بشأن
النظام الإماراتي للمركبات الهيدروجينية
( الملحق رقم2
) بشأن المواصفات القياسية الخاصة بالمركبات الهيدروجينية
المرفق ب( قرار مجلس الوزراء رقم42) لسنة
2021
بشأن النظام الإماراتي للمركبات الهيدروجينية
Standards Title
Standard No.
Vehicle Fuel System
Compressed hydrogen surface vehicle refuelling connection devices
UAE.S ISO 17268
Fuel cell road vehicles – Safety specifications – Part 1: Vehicle functional
safety;
UAE.S ISO 23273-1
Fuel cell road vehicles – Safety specifications – Part 2: Protection against
hydrogen hazards for vehicles fuelled with compressed hydrogen
UAE.S ISO 23273-2
Hydrogen fuel quality — Product specification
UAE.S ISO 14687
Storage System
Implementing of type-approval of hydrogen-powered motor vehicles
EU Regulation 406/2010
Liquid Hydrogen – Land Vehicle Fuel Tanks
UAE.S ISO 13985:2006
Gaseous Hydrogen and Hydrogen Blends – Land Vehicle Fuel Tanks
(Technical Specification)
UAE.S ISO 15869:2009
Electric Safety Regulations
The approval of vehicles with regard to specific requirements for the
electric power train
UAE.S ECE R 100
Electric-Powered Vehicles: Electrolyte Spillage and Electrical Shock
Protection
UAE.S FMVSS 305
Fuel cell road vehicles — Safety specifications – Part 3: Protection of
persons against electric shock;
UAE.S ISO 23273-3
Gaseous hydrogen - Fuelling stations - Part 3: Valves
UAE.S ISO 19880-3:2018
Gaseous hydrogen - Fuelling stations - Part 1: General requirements
UAE.S ISO 19880-1:2020
ملاحظة : يتم قبوو مواصفاتFMVSS
.كمواصفات مكافئة للمواصفات المعتمدة
12
قرار مجلس الوزراء
لسنة2021
بشأن
النظام الإماراتي للمركبات الهيدروجينية
( الملحق رقم3
) بشأن المتطلبات الفنية الإماراتية للمركبات الهيدروجينية
المرفق بقرار مجلس الوزراء رقم(
42
) لسنة2021
بشأن النظام الإماراتي للمركبات الهيدروجينية
Technical regulation on hydrogen fueled vehicles
1. Scope
This regulation applies to all hydrogen fuelled vehicles with a gross vehicle mass (GVM) of 4,500
kilograms or less and a speed not less than 25 Km/h.
2. Definitions
For the purpose of this regulation, the following definitions shall apply:
2.1.
"Active driving possible mode" is the vehicle mode when application of pressure to the accelerator
pedal (or activation of an equivalent control) or release of the brake system causes the electric power
train to move the vehicle
3.2.
"Automatic disconnect" is a device that, when triggered, conductively separates the electrical energy
sources from the rest of the high voltage circuit of the electrical power train.
3.3.
"Burst-disc" is the non-reclosing operating part of a pressure relief device which, when installed in the
device, is designed to burst at a predetermined pressure to permit the discharge of compressed
hydrogen.
3.4.
"Check valve" is a non-return valve that prevents reverse flow in the vehicle fuel line.
3.5.
"Concentration of hydrogen" is the percentage of the hydrogen moles (or molecules) within the
mixture of hydrogen and air (Equivalent to the partial volume of hydrogen gas).
3. 6
"Container" (for hydrogen storage) is the component within the hydrogen storage system that stores
the primary volume of hydrogen fuel.
3.7.
"Conductive connection" is the connection using contactors to an external power supply when the
rechargeable energy storage system (REESS) is charged.
3.8.
"Coupling system" for charging the rechargeable energy storage system (REESS) is the electrical circuit
used for charging the REESS from an external electric power supply including the vehicle inlet.
3.9.
"Date of removal from service" is the date (month and year) specified for removal from service.
3.10. "Date of manufacture" (of a compressed hydrogen container) is the date (month and year) of the proof
pressure test carried out during manufacture.
3.11. "Direct contact" indicates the contact of persons with high voltage live parts.
3.12. "Enclosed or semi-enclosed spaces” indicates the special volumes within the vehicle (or the vehicle
outline across openings), that are external to the hydrogen system (storage system, fuel cell system and
fuel flow management system) and its housings (if any) where hydrogen may accumulate (and thereby
pose a hazard), as it may occur in the passenger compartment, luggage compartment, cargo
compartment and space under the hood.
3.13. "Enclosure" is the part enclosing the internal units and providing protection against any direct contact.
13
قرار مجلس الوزراء
لسنة2021
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النظام الإماراتي للمركبات الهيدروجينية
3.14. "Electric energy conversion system" is a system (e.g. fuel cell) that generates and provides electrical
power for vehicle propulsion.
3.15. "Electric power train" is the electrical circuit which may include the traction motor(s), and may also
include the REESS, the electrical power conversion system, the electronic converters, the traction
motors, the associated wiring harness and connectors and the coupling system for charging the REESS.
3.16. "Electrical chassis" is a set of conductive parts electrically linked together, whose electrical potential is
taken as reference.
3.17. "Electrical circuit" is an assembly of connected high voltage live parts that is designed to be electrically
energized in normal operation.
3.18. "Electrical isolation" is the electrical resistance between a vehicle high voltage bus source and any
vehicle conductive structure.
3.19. "Electrical protection barrier" is the part providing protection against direct contact with live parts from
any direction of access.
3.20. "Electronic converter" is a device capable of controlling and/or converting electric power for
propulsion.
3.21. "Exhaust point of discharge" is the geometric centre of the area where fuel cell purged gas is discharged
from the vehicle.
3.22. "Exposed conductive part" is the conductive part that can be touched under the provisions of the IPXXB
protection degree and becomes electrically energized under isolation failure conditions. This includes
parts under a cover that can be removed without using tools.
3.23. "External electric power supply" is an alternating current (AC) or direct current (DC) that provides
electric power outside of the vehicle.
3.24. "Fuel cell system" is a system containing the fuel cell stack(s), air processing system, fuel flow control
system, exhaust system, thermal management system and water management system.
3.25. "Fuelling receptacle" is the equipment to which a fuelling station nozzle attaches to the vehicle and
through which fuel is transferred to the vehicle. The fuelling receptacle is used as an alternative to a
fuelling port.
3.26. "High voltage" is the classification of an electric component or circuit, if its maximum working voltage
is greater than 60 V and less than or equal to 1500 V of direct current (DC), or greater than 30 V and
less than or equal to 1000 V of alternating current (AC).
3.27. "High Voltage Bus" is the electrical circuit, including the coupling system, for charging the REESS that
operates on high voltage.
3.28. "Hydrogen-fuelled vehicle" indicates any motor vehicle that uses compressed gaseous or liquefied
hydrogen as a fuel to propel the vehicle, including fuel cell and internal combustion engine vehicles.
Hydrogen fuel for passenger vehicles is specified in UAE.S ISO 14687 and SAE J2719.
3.29. "Hydrogen storage system" indicates a pressurized container, pressure relief devices (PRDs) and shut
off device that isolate the stored hydrogen from the remainder of the fuel system and the environment.
14
قرار مجلس الوزراء
لسنة2021
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النظام الإماراتي للمركبات الهيدروجينية
3.30. "Indirect contact" is the contact of persons with exposed conductive parts.
3.31. "Live parts" is the conductive part intended to be electrically energized in normal use.
3.32. "Luggage compartment" is the space in the vehicle for luggage accommodation, bounded by the roof,
hood, floor, side walls, as well as by the electrical barrier and enclosure provided for protecting the
power train from direct contact with live parts, being separated from the passenger compartment by
the front bulkhead or the rear bulkhead.
3.33. "Liquefied hydrogen storage system" indicates liquefied hydrogen storage container(s) PRDs, shut off
device, a boil-off system and the interconnection piping (if any) and fittings between the above
components.
3.34. "Lower flammability limit (LFL)" is the lowest concentration of fuel at which a gaseous fuel mixture is
flammable at normal temperature and pressure. The lower flammability limit for hydrogen gas in air is
4 per cent by volume ( 83 of the Preamble).
3.35. "Maximum allowable working pressure (MAWP)" is the highest gauge pressure to which a pressure
container or storage system is permitted to operate under normal operating conditions.
3.36 "Maximum fuelling pressure (MFP)" is the maximum pressure applied to compressed system during
fuelling. The maximum fuelling pressure is 125 per cent of the Nominal Working Pressure.
3.37. "Nominal working pressure (NWP)" is the gauge pressure that characterizes typical operation of a
system. For compressed hydrogen gas containers, NWP is the settled pressure of compressed gas in
fully fuelled container or storage system at a uniform temperature of 15 °C.
3.38. "On-board isolation resistance monitoring system" is the device that monitors isolation resistance
between the high voltage buses and the electrical chassis.
3.39. "Open type traction battery" is a type of battery requiring liquid and generating hydrogen gas that is
released into the atmosphere.
3.40. "Passenger compartment (for electric safety assessment)" is the space for occupant accommodation,
bounded by the roof, floor, side walls, doors, outside glazing, front bulkhead and rear bulkhead - or rear
gate -, as well as by the electrical barriers and enclosures provided for protecting the occupants from
direct contact with live parts.
3.41. "Pressure relief device (PRD)" is a device that, when activated under specified performance conditions,
is used to release hydrogen from a pressurized system and thereby prevent failure of the system.
3.42. "Pressure relief valve" is a pressure relief device that opens at a pre-set pressure level and can re-close.
3.43. "Protection degree IPXXB" indicates protection from contact with high voltage live parts provided by
either an electrical barrier or an enclosure; it is tested using a Jointed Test Finger (IPXXB), as described
in paragraph ANNEX 1.3.3.
3.44. "Protection degree IPXXD" indicates protection from contact with high voltage live parts provided by
either an electrical barrier or an enclosure and tested using a Test Wire (IPXXD), as described in
paragraph ANNEX 1.3.3.
15
قرار مجلس الوزراء
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النظام الإماراتي للمركبات الهيدروجينية
3.45. "Rechargeable energy storage system (REESS)" is the rechargeable energy storage system that provides
electric energy for electrical propulsion.
3.46 "Rupture and burst" both mean to come apart suddenly and violently, break open or fly into pieces due
to the force of internal pressure.
3.47. "Service disconnect" is the device for deactivation of an electrical circuit when conducting checks and
services of the REESS, fuel cell stack, etc.
3.48. "Service life" (of a compressed hydrogen container) indicates the time frame during which service
(usage) is authorized.
3.49. "Shut-off valve" is a valve between the storage container and the vehicle fuel system that can be
automatically activated; this valve defaults to "closed" position when not connected to a power source.
3.50. "Single failure" is a failure caused by a single event, including any consequential failures resulting from
this failure.
3.51. "Solid insulator" is the insulating coating of wiring harnesses provided in order to cover and prevent
the high voltage live parts from any direct contact. This includes covers for insulating the high voltage
live parts of connectors and varnish or paint for the purpose of insulation.
3.52. "Thermally-activated pressure relief device (TPRD)" is a non- reclosing PRD that is activated by
temperature to open and release hydrogen gas.
3.53. "Type approval" indicates a certification of a recognised body stating that prototype or pre-production
samples of a specific vehicle, vehicle system or vehicle system component meet the relevant specified
performance standards, and that the final production versions also comply, as long as conformity of
production is confirmed.
3.54. "Vehicle fuel system" is an assembly of components used to store or supply hydrogen fuel to a fuel cell
(FC) or internal combustion engine (ICE).
3.55. "Working voltage" is the highest value of an electrical circuit voltage root mean square (rms), specified
by the manufacturer or determined by measurement, which may occur between any conductive parts
in open circuit conditions or under normal operating condition. If the electrical circuit is divided by
galvanic isolation, the working voltage is defined for each divided circuit, respectively.
4. Applicability of requirements
4.1.
The requirements of paragraph 5. (Using test conditions and procedures in paragraph ANNEX 1.) Apply to
all compressed hydrogen fuelled vehicles.
4.2.
Crash tests (frontal, side, rear and rollover) for compliance with section 5.2.2. should be according GSO 42.
4.3.
The requirements of paragraph 5.3. Apply to all hydrogen-fuelled vehicles using high voltage.
5. Performance requirements
5.1.
Compressed hydrogen storage system
This section specifies the requirements for the integrity of the compressed hydrogen storage system.
The hydrogen storage system consists of the high pressure storage container and primary closure
devices for openings into the high pressure storage container. Figure 1 shows a typical compressed
hydrogen storage system
16
قرار مجلس الوزراء
لسنة2021
بشأن
النظام الإماراتي للمركبات الهيدروجينية
Figure 1
Typical compressed hydrogen storage system
All new compressed hydrogen storage systems produced for on-road vehicle service shall have a NWP of 70
MPa or less and a service life of 15 years or less, and be capable of satisfying the requirements of
paragraph 5.1.
The hydrogen storage system shall meet the performance test requirements specified in this paragraph.
The test elements within these performance requirements are summarized in Table 1. The corresponding test
procedures are specified in paragraph ANNEX 1.
Table 1
Overview of performance qualification test requirements
5.1.1. Verification tests for baseline metrics
5.1.1.1. Baseline initial burst pressure
5.1.1.2. Baseline initial pressure cycle life
5.1.2. Verification test for performance durability (sequential hydraulic tests)
5.1.2.1. Proof pressure test
5.1.2.2. Drop (impact) test
5.1.2.3. Surface damage
5.1.2.4. Chemical exposure and ambient temperature pressure cycling tests
5.1.2.5. High temperature static pressure test
5.1.2. ANNEX 1. Extreme temperature pressure cycling
5.1.2.7. Residual proof pressure test
5.1.2.8. Residual strength Burst Test
5.1.3. Verification test for expected on-road performance (sequential pneumatic
tests)
5.1.3.1. Proof pressure test
5.1.3.2. Ambient and extreme temperature gas pressure cycling test (pneumatic)
5.1.3.3. Extreme temperature static gas pressure leak/permeation test (pneumatic)
5.1.3.4. Residual proof pressure test
5.1.3.5. Residual strength burst test (hydraulic)
Containment
Vessel
Shut-off
Valve
Check
Valve
TPRD
vent
Storage
Container
Containment
Vessel
Shut-off
Valve
Check
Valve
TPRD
vent
Storage
Container
17
قرار مجلس الوزراء
لسنة2021
بشأن
النظام الإماراتي للمركبات الهيدروجينية
5.1.1. Verification tests for baseline metrics
5.1.1.1. Baseline initial burst pressure
5.1.1.2. Baseline initial pressure cycle life
5.1.4. Verification test for service terminating performance in fire
5.1.5. Verification test for closure durability
5.1.1. Verification tests for baseline metrics
5.1.1.1. Baseline initial burst pressure
Three (3) new containers randomly selected from the design qualification batch of at least 10
containers, are hydraulically pressurized until burst ( ANNEX 1.2.2.1. test procedure). The
manufacturer shall supply documentation (measurements and statistical analyses) that establish the
midpoint burst pressure of new storage containers, BPO.
All containers tested shall have a burst pressure within ±10 per cent of BPO and greater than or equal
to a minimum BPmin of 225 per cent NWP.
In addition, containers having glass-fibre composite as a primary constituent to have a minimum burst
pressure greater than 350 per cent NWP.
5.1.1.2. Baseline initial pressure cycle life
Three (3) new containers randomly selected from the design qualification batch are hydraulically
pressure cycled at 20(±5(°C to 125 per cent NWP without rupture for 22,000 cycles or until a leak
occurs ( ANNEX 1.2.2.2. test procedure). Leakage shall not occur within a number of Cycles, where
the number of Cycles is set individually by each Contracting Party at 5,500, 7,500 or 11,000 cycles for
a 15-year service life.
5.1.2. Verification tests for performance durability (Hydraulic sequential tests)
If all three pressure cycle life measurements made in 5.1.1.2. are greater than 11,000 cycles, or if they
are all within ±25 per cent of each other, then only one (1) container is tested in 5.1.2. Otherwise,
three (3) containers are tested in 5.1.2.
A hydrogen storage container shall not leak during the following sequence of tests, which are applied
in series to a single system and which are illustrated in Figure 2. At least one system randomly selected
from the design qualification batch shall be tested to demonstrate the performance capability. Specifics
of applicable test procedures for the hydrogen storage system are provided in ANNEX 1.2.3.
Figure 2
Verification test for performance durability (hydraulic)
18
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النظام الإماراتي للمركبات الهيدروجينية
5.1.2.1. Proof pressure test
A storage container is pressurized to 150 per cent NWP and held for 30 sec ( ANNEX 1.2.3.1. test procedure).
A storage container that has undergone a proof pressure test in manufacture is exempt from this test.
5.1.2.2. Drop (impact) test
The storage container is dropped at several impact angles ( ANNEX 1.2.3.2. test procedure).
5.1.2.3. Surface damage test
The storage container is subjected to surface damage ( ANNEX 1.2.3.3. test procedure).
5.1.2.4. Chemical exposure and ambient-temperature pressure cycling test
The storage container is exposed to chemicals found in the on-road environment and pressure cycled to 125
per cent NWP at 20° )±5(°C for 60 per cent number of Cycles pressure cycles ( ANNEX 1.2.3.4. test
procedure). Chemical exposure is discontinued before the last 10 cycles, which are conducted to 150
per cent NWP.
5.1.2.5. High temperature static pressure test.
The storage container is pressurized to 125 per cent NWP at 85°C for 1,000 hr ( ANNEX 1.2.3.5. test
procedure).
5.1.2. ANNEX 1. Extreme temperature pressure cycling.
The storage container is pressure cycled at -40°C to 80 per cent NWP for 20 per cent number of Cycles and
at +85°C and 95 per cent relative humidity to 125 per cent NWP for 20 per cent number of Cycles
( ANNEX 1.2.2.2. test procedure).
5.1.2.7. Hydraulic residual pressure test. The storage container is pressurized to 180 per cent NWP and held 4
minutes without burst ( ANNEX 1.2.3.1. test procedure).
5.1.2.8. Residual burst strength test
The storage container undergoes a hydraulic burst test to verify that the burst pressure is at least 80 per cent
of the baseline initial burst pressure (BPO) determined in 5.1.1.1. ( ANNEX 1.2.2.1. test procedure).
5.1.3. Verification test for expected on-road performance (Pneumatic sequential tests)
+85C, 95%RH
Pressure →
Damage
Drop
time
BPO
<20%
Residual
Strength
Chemicals
48 hr
60% #Cycles
15C-25C
chemical
exposure
150% NWP
burst
125%NWP
180%NWP
(4 min)
1000 hr
+85C
20% #Cycles
-40C
20% #Cycles
10
cycles
15-25C
Proof Pressure
80%NWP
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A hydrogen storage system shall not leak during the following sequence of tests, which are illustrated in Figure
3. Specifics of applicable test procedures for the hydrogen storage system are provided in paragraph
ANNEX 1.
Figure 3
Verification test for expected on-road performance (pneumatic/hydraulic)
5.1.3.1. Proof pressure test
A system is pressurized to 150 per cent NWP for 30 seconds ( ANNEX 1.2.3.1. test procedure). A
storage container that has undergone a proof pressure test in manufacture is exempt from this test.
5.1.3.2. Ambient and extreme temperature gas pressure cycling test
The system is pressure cycled using hydrogen gas for 500 cycles ( ANNEX 1.2.4.1. test procedure).
(a)
The pressure cycles are divided into two groups: Half of the cycles (250) are performed before exposure
to static pressure ( 5.1.3.3.) and the remaining half of the cycles (250) are performed after the initial
exposure to static pressure ( 5.1.3.3.) as illustrated in Figure 3;
(b)
The first group of pressure cycling, 25 cycles are performed to 80 per cent NWP at -40 °C, then 25
cycles to 125 per cent NWP at + 50 °C and 95 per cent relative humidity, and the remaining
200 cycles to 125 per cent NWP at 20 (±5)°C;
The second group of pressure cycling, 25 cycles are performed to 125 per cent NWP at + 50 °C and
95 per cent relative humidity, then 25 cycles to 80 per cent NWP at -40 °C, and the remaining
200 cycles to 125 per cent NWP at 20)±5(°C.
(c)
The hydrogen gas fuel temperature is - 40 °C;
(d)
During the first group of 250 pressure cycles, five cycles are performed with fuel having a temperature
of + 20)±5(°C after temperature equilibration of the system at - 40°C; five cycles are performed with
fuel having a temperature of - 40°C; and five cycles are performed with fuel having a temperature of
- 40°C after temperature equilibration of the system at 50°C and 95 per cent relative humidity;
c
b
Proof Pressure
5% cy -40Ca
5% cy +50Cb
40%cy 15-25Cc
150%
NWP
+55oC
+55oC
a
Pressure →
time
Burst
BPO
<20%
Leak / Permeation
> 30 hrs
a Fuel/defuel cycles @-40oC with initial system equilibration @ -40oC, 5 cycles with +20oC fuel; 5 cycles with <-35oC fuel
b Fuel/defuel cycles @+50oC with initial system equilibration @+50oC, 5 cycles with <-35oC fuel
c Fuel/defuel cycles @15-25oC with service (maintenance) defuel rate, 50 cycles
5% cy +50C
5% cy -40C
40%cy 15-25C
Leak / Permeation
> 30 hrs
180%NWP
4 min
125%NWP
115%NWP
80%NWP
a
b
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(e)
Fifty pressure cycles are performed using a de-fuelling rate greater than or equal to the maintenance
de-fuelling rate.
5.1.3.3. Extreme temperature static pressure leak/permeation test.
(a)
The test is performed after each group of 250 pneumatic pressure cycles in paragraph 5.1.3.2.;
(b)
The maximum allowable hydrogen discharge from the compressed hydrogen storage system is 46
mL/h/L water capacity of the storage system. ( ANNEX 1.2.4.2. Test procedure);
(c)
If the measured permeation rate is greater than 0.005 mg/sec (3.6 Nml/min), a localized leak test is
performed to ensure no point of localized external leakage is greater than 0.005 mg/sec (3.6 Nml/min)
( ANNEX 1.2.4.3. test procedure).
5.1.3.4. Residual proof pressure test (hydraulic)
The storage container is pressurized to 180 per cent NWP and held 4 minutes without burst ( ANNEX
1.2.3.1. test procedure).
5.1.3.5. Residual strength burst test (hydraulic)
The storage container undergoes a hydraulic burst to verify that the burst pressure is within 20 per cent
of the baseline burst pressure determined in 5.1.1.1. ( ANNEX 1.2.2.1. test procedure).
5.1.4. Verification test for service terminating performance in fire
This section describes the fire test with compressed hydrogen as the test gas.
A hydrogen storage system is pressurized to NWP and exposed to fire ( ANNEX 1.2.5.1. test
procedure). A temperature-activated pressure relief device shall release the contained gases in a
controlled manner without rupture.
5.1.5. Verification test for performance durability of primary closures
Manufacturers shall maintain records that confirm that closures that isolate the high pressure
hydrogen storage system (the TPRD(s), check valve(s) and shut-off valve(s) shown in Figure 1) comply
with the requirements described in the remainder of this Section.
The entire storage system does not have to be re-qualified ( 5.1.) if these closure components
(components in Figure 1 excluding the storage container) are exchanged for equivalent closure
components having comparable function, fittings, materials, strength and dimensions, and qualified
for performance using the same qualification tests as the original components. However, a change in
TPRD hardware, its position of installation or venting lines requires re-qualification with fire testing
according to 5.1.4.
5.1.5.1. TPRD qualification requirements
Design qualification testing shall be conducted on finished pressure relief devices, which are
representative of normal production. The TPRD shall meet the following performance qualification
requirements:
(a)
Pressure cycling test ( ANNEX 1.2. ANNEX 1.1.1.);
(b)
Accelerated life test ( ANNEX 1.2. ANNEX 1.1.2.);
(c)
Temperature cycling test ( ANNEX 1.2. ANNEX 1.1.3.);
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(d)
Salt corrosion resistance test ( ANNEX 1.2. ANNEX 1.1.4.);
(e)
Vehicle environment test ( ANNEX 1.2. ANNEX 1.1.5.);
(f)
Stress corrosion cracking test ( ANNEX 1.2. ANNEX 1.1. ANNEX 1.);
(g)
Drop and vibration test ( ANNEX 1.2. ANNEX 1.1.7.);
(h)
Leak test ( ANNEX 1.2. ANNEX 1.1.8.);
(i)
Bench top activation test ( ANNEX 1.2. ANNEX 1.1.9.);
(j)
Flow rate test ( ANNEX 1.2. ANNEX 1.1.10.).
5.1.5.2. Check valve and automatic shut-off valve qualification on requirements
Design qualification testing shall be conducted on finished check valves and shut-off valves which are
representative of normal production. The valve units shall meet the following performance
qualification requirements:
(a)
Hydrostatic strength test ( ANNEX 1.2. ANNEX 1.2.1.);
(b)
Leak test ( ANNEX 1.2. ANNEX 1.2.2.);
(c)
Extreme temperature pressure cycling test ( ANNEX 1.2. ANNEX 1.2.3.);
(d)
Salt corrosion resistance test ( ANNEX 1.2. ANNEX 1.2.4.);
(e)
Vehicle environnement test ( ANNEX 1.2. ANNEX 1.2.5.);
(f)
Atmospheric exposure test ( ANNEX 1.2. ANNEX 1.2. ANNEX 1.);
(g)
Electrical tests ( ANNEX 1.2. ANNEX 1.2.7.);
(h)
Vibration test ( ANNEX 1.2. ANNEX 1.2.8.);
(i)
Stress corrosion cracking test ( ANNEX 1.2. ANNEX 1.2.9.);
(j)
Pre-cooled hydrogen exposure test ( ANNEX 1.2. ANNEX 1.2.10.).
5.1. ANNEX 1.
Labelling
A label shall be permanently affixed on each container with at least the following information: name
of the manufacturer, serial number, date of manufacture, NWP, type of fuel, and date of removal from
service. Each container shall also be marked with the number of cycles used in the testing programme
as per 5.1.1.2. Any label affixed to the container in compliance with this section shall remain in place
and be legible for the duration of the manufacturer’s recommended service life for the container.
Date of removal from service shall not be more than 15 years after the date of manufacture.
5.2.
Vehicle fuel system
This section specifies requirements for the integrity of the hydrogen fuel delivery system, which includes the
hydrogen storage system, piping, joints, and components in which hydrogen is present.
5.2.1. In-use fuel system integrity
5.2.1.1. Fuelling receptacle requirements
5.2.1.1.1. A compressed hydrogen fuelling receptacle shall prevent reverse flow to the atmosphere. Test
procedure is visual inspection.
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5.2.1.1.2. Fuelling receptacle label A label shall be affixed close to the fuelling receptacle; for instance, inside a
refilling hatch, showing the following information: fuel type, NWP, date of removal from service of
containers.
5.2.1.1.3. The fuelling receptacle shall be mounted on the vehicle to ensure positive locking of the fuelling
nozzle. The receptacle shall be protected from tampering and the ingress of dirt and water (e.g. installed
in a compartment which can be locked). Test procedure is by visual inspection.
5.2.1.1.4. The fuelling receptacle shall not be mounted within the external energy absorbing elements of the
vehicle (e.g. bumper) and shall not be installed in the passenger compartment, luggage compartment
and other places where hydrogen gas could accumulate and where ventilation is not sufficient. Test
procedure is by visual inspection.
5.2.1.2. Over-pressure protection for the low pressure system ( ANNEX 1.1. ANNEX 1. test procedure)
The hydrogen system downstream of a pressure regulator shall be protected against overpressure due
to the possible failure of the pressure regulator. The set pressure of the overpressure protection device
shall be lower than or equal to the maximum allowable working pressure for the appropriate section
of the hydrogen system.
5.2.1.3. Hydrogen discharge systems
5.2.1.3.1.Pressure relief systems ( ANNEX 1.1. ANNEX 1. test procedure)
(a)
Storage system TPRDs. The outlet of the vent line, if present, for hydrogen gas discharge from TPRD(s)
of the storage system shall be protected by a cap;
(b)
Storage system TPRDs. The hydrogen gas discharge from TPRD(s) of the storage system shall not be
directed:
(i)
Into enclosed or semi-enclosed spaces;
(ii)
Into or towards any vehicle wheel housing;
(iii)
Towards hydrogen gas containers;
(iv)
Forward from the vehicle, or horizontally (parallel to road) from the back or sides of the vehicle.
(c)
Other pressure relief devices (such as a burst disk) may be used outside the hydrogen storage system.
The hydrogen gas discharge from other pressure relief devices shall not be directed:
(i)
Towards exposed electrical terminals, exposed electrical switches or other ignition sources;
(ii)
Into or towards the vehicle passenger or cargo compartments;
(iii)
Into or towards any vehicle wheel housing;
(iv)
Towards hydrogen gas containers.
5.2.1.3.2. Vehicle Exhaust System (ANNEX 1.1.4. test procedure)
At the vehicle exhaust system’s point of discharge, the hydrogen concentration level shall:
(a)
Not exceed 4 per cent average by volume during any moving three-second time interval during normal
operation including start-up and shutdown;
(b)
And not exceed 8 per cent at any time (ANNEX 1.1.4. test procedure).
5.2.1.4. Protection against flammable conditions: single failure conditions
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5.2.1.4.1. Hydrogen leakage and/or permeation from the hydrogen storage system shall not directly vent into
the passenger, luggage, or cargo compartments, or to any enclosed or semi-enclosed spaces within the
vehicle, that contains unprotected ignition sources.
5.2.1.4.2. Any single failure downstream of the main hydrogen shut off valve shall not result in any level of a
hydrogen concentration in anywhere in the passenger compartment according to test
procedure ANNEX 1.1.3.2.
5.2.1.4.3. If, during operation, a single failure results in a hydrogen concentration exceeding 2 ± 1.0 per cent
by volume in air in the enclosed or semi-enclosed spaces of the vehicle, then a warning shall be
provided ( 5.2.1. ANNEX 1.). If the hydrogen concentration exceeds 3 ± 1.0 per cent by volume in the
air in the enclosed or semi-enclosed spaces of the vehicle, the main shutoff valve shall be closed to
isolate the storage system. ( ANNEX 1.1.3. test procedure).
5.2.1.5. Fuel system leakage
The hydrogen fuelling line and the hydrogen system(s) downstream of the main shut off valve(s)
shall not leak. Compliance shall be verified at NWP ( ANNEX 1.1.5. test procedure).
5.2.1. ANNEX 1. Tell-tale signal warning to driver
The warning shall be given by a visual signal or display text with the following properties:
(a)
Visible to the driver while in the driver's designated seating position with the driver's seat belt fastened;
(b)
Yellow in colour if the detection system malfunctions and shall be red in compliance with section
5.2.1.4.3;
(c)
When illuminated, shall be visible to the driver under both daylight and night time driving conditions;
(d)
Remains illuminated when 2 ± 1.0 per cent concentration or detection malfunction) exists and the
ignition locking system is in the "On" ("Run") position or the propulsion system is activated.
5.2.2. Post-crash fuel system integrity
5.2.2.1. Fuel leakage limit
The volumetric flow of hydrogen gas leakage shall not exceed an average of 118 NL per minute for 60 minutes
after the crash ( ANNEX 1.1.1. test procedures).
5.2.2.2. Concentration limit in enclosed spaces
Hydrogen gas leakage shall not result in a hydrogen concentration in the air greater than 3 ± 1.0 per cent] by
volume in the passenger, luggage and cargo compartments ( ANNEX 1.1.2. test procedures). The
requirement is satisfied if it is confirmed that the shut-off valve of the storage system has closed within
5 seconds of the crash and no leakage from the storage system.
5.2.2.3. Container Displacement
The storage container(s) shall remain attached to the vehicle at a minimum of one attachment point.
5.3.
Electrical safety
5.3.1. Electrical Safety requirements - in-use
5.3.1.1. General
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Paragraph 5.3.1. applies to the electric power train of fuel cell vehicles equipped with one or more traction
motor(s) operated by electric power and not permanently connected to the grid, as well as their high
voltage components and systems which are conductively connected to the high voltage bus of the
electric power train.
5.3.1.2. Requirements for protection against electric shock
5.3.1.2.1. Protection against electric shock
These electrical safety requirements apply to high voltage buses under conditions where they are not
connected to external high voltage power supplies.
5.3.1.2.2. Protection against direct contact
The protection against direct contact with live parts shall comply with paragraphs 5.3.1.2.2.1. and 5.3.1.2.2.2.
These protections (solid insulator, electrical protection barrier, enclosure, etc.) shall not be opened,
disassembled or removed without the use of tools.
5.3.1.2.2.1. For protection of live parts inside the passenger compartment or luggage compartment, the
protection degree IPXXD shall be provided.
5.3.1.2.2.2. For protection of live parts in areas other than the passenger compartment or luggage
compartment, the protection degree IPXXB shall be satisfied.
5.3.1.2.2.3. Connectors
Connectors (including vehicle inlet) are deemed to meet this requirement if:
(a)
They comply with paragraphs 5.3.1.2.2.1. and 5.3.1.2.2.2. when separated without the use of tools; or
(b)
They are located underneath the floor and are provided with a locking mechanism; or
(c)
They are provided with a locking mechanism and other components shall be removed with the use of
tools in order to separate the connector; or
(d)
The voltage of the live parts becomes equal or below DC 60V or equal or below AC 30V (rms) within 1
second after the connector is separated.
5.3.1.2.2.4. Service disconnect
For a service disconnect which can be opened, disassembled or removed without tools, it is acceptable
if protection degree IPXXB is satisfied when it is opened, disassembled or removed without tools.
5.3.1.2.2.5. Marking
5.3.1.2.2.5.1. The symbol shown in Figure 4 shall appear on or near the REESS. The symbol background shall
be yellow, the bordering and the arrow shall be black.
Figure 4
Marking of high voltage equipment
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5.3.1.2.2.5.2. The symbol shall be visible on enclosures and electrical protection barriers, which, when
removed, expose live parts of high voltage circuits. This provision is optional to any connectors for high
voltage buses. This provision shall not apply to any of the following cases
(a)
Where electrical protection barriers or enclosures cannot be physically accessed, opened, or removed;
unless other vehicle components are removed with the use of tools;
(b)
Where electrical protection barriers or enclosures are located underneath the vehicle floor.
5.3.1.2.2.5.3. Cables for high voltage buses which are not located within enclosures shall be identified by
having an outer covering with the colour orange.
5.3.1.2.3. Protection against indirect contact
5.3.1.2.3.1. For protection against electric shock which could arise from indirect contact, the exposed
conductive parts, such as the conductive electrical protection barrier and enclosure, shall be
conductively connected and secured to the electrical chassis with electrical wire or ground cable, by
welding, or by connection using bolts, etc. so that no dangerous potentials are produced.
5.3.1.2.3.2. The resistance between all exposed conductive parts and the electrical chassis shall be lower
than 0.1ohm when there is current flow of at least 0.2 amperes. Demonstrated by using one of the
test procedures described in ANNEX 1.3.4.
This requirement is satisfied if the galvanic connection has been established by welding. In case of
doubts a measurement shall be made.
5.3.1.2.3.3. In the case of motor vehicles which are connected to the grounded external electric power supply
through the conductive connection, a device to enable the conductive connection of the electrical
chassis to the earth ground shall be provided.
The device shall enable connection to the earth ground before exterior voltage is applied to the vehicle
and retain the connection until after the exterior voltage is removed from the vehicle.
Compliance to this requirement may be demonstrated either by using the connector specified by the
car manufacturer, or by analysis (e.g. visual inspection, drawings etc.).
5.3.1.2.4. Isolation resistance monitoring system
5.3.1.2.4.1. In fuel cell vehicles, DC high voltage buses shall have an on-board isolation resistance monitoring
system together with a warning to the driver if the isolation resistance drops below the minimum
required value of 100 ohms/volt. The function of the on-board isolation resistance monitoring system
shall be confirmed as described in ANNEX 1.3.2.
The isolation resistance between the high voltage bus of the coupling system for charging the REESS,
which is not energized in conditions other than that during the charging of the REESS, and the electrical
chassis need not to be monitored.
5.3.1.2.4.2. Electric power train consisting of separate DC or AC buses
If AC high voltage buses and DC high voltage buses are conductively isolated from each other,
isolation resistance between the high voltage bus and the electrical chassis shall have a minimum value
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of 100 ohms/volt of the working voltage for DC buses, and a minimum value of 500 ohms/volt of the
working voltage for AC buses. The measurement shall be conducted according to ANNEX 1.3.1.
5.3.1.2.4.3. Electric power train consisting of combined DC- and AC-buses
If AC high voltage buses and DC high voltage buses are galvanically connected, isolation resistance between
the high voltage bus and the electrical chassis shall have a minimum value of 500 Ω/volt of the working
voltage.
However, if all AC high voltage buses are protected by one of the two following measures, isolation
resistance between the high voltage bus and the electrical chassis shall have a minimum value of 100
ohms/volt of the working voltage.
(a)
Double or more layers of solid insulators, electrical protection barriers or enclosures that meet the
requirement in paragraph 5.3.1.2.3. independently, for example wiring harness;
(b)
Mechanically robust protections that have sufficient durability over vehicle service life such as motor
housings, electronic converter cases or connectors.
5.3.1.2.4.4. Isolation resistance requirement for the coupling system for charging the REESS.
For the vehicle inlet intended to be conductively connected to the grounded external AC power supply and the
electrical circuit that is conductively connected to the vehicle inlet during charging the REESS, the
isolation resistance between the high voltage bus and the electrical chassis shall be at least 1M ohms
when the charger coupler is disconnected. During the measurement, the REESS may be disconnected.
The measurement shall be conducted according to ANNEX 1.3.1.
5.3.1.3. Functional safety
At least a momentary indication shall be given to the driver when the vehicle is in "active driving
possible mode''.
However, this provision does not apply under conditions where an internal combustion engine
provides directly or indirectly the vehicle´s propulsion power upon start up.
When leaving the vehicle, the driver shall be informed by a signal (e.g. optical or audible signal) if the
vehicle is still in the active driving possible mode.
If the on-board REESS can be externally charged, vehicle movement by its own propulsion system
shall be impossible as long as the connector of the external electric power supply is physically
connected to the vehicle inlet.
This requirement shall be demonstrated by using the connector specified by the car manufacturer.
The state of the drive direction control unit shall be identified to the driver.
5.3.2. Electric safety requirements – post-crash
5.3.2.1. General
Fuel cell vehicles equipped with electric power train shall comply with the requirements of paragraphs
5.3.2.2. to 5.3.2.4. This can be met by a separate impact test provided that the electrical components
do not influence the occupant protection performance of the vehicle type as defined in the impact
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regulation. In case of this condition the requirements of paras. 5.3.2.2. to 5.3.2.4. shall be checked in
accordance with the methods set out in ANNEX 1.3.5.
5.3.2.2. Protection against electric shock
After the impact at least one of the three criteria specified in paragraphs 5.3.2.2.1. to 5.3.2.2.3. shall be
met.
If the vehicle has an automatic disconnect function, or device(s) that conductively divide the electric
power train circuit during driving condition, at least one of the following criteria shall apply to the
disconnected circuit or to each divided circuit individually after the disconnect function is activated.
However criteria defined in 5.3.2.2.2. shall not apply if more than a single potential of a part of the
high voltage bus is not protected under the conditions of protection degree IPXXB.
In the case that the test is performed under the condition that part(s) of the high voltage system are not
energized, the protection against electric shock shall be proved by either 5.3.2.2.2. or 5.3.2.2.3. for
the relevant part(s).
5.3.2.2.1. Absence of high voltage
The voltages Vb, V1 and V2 of the high voltage buses shall be equal or less than 30 VAC or 60 VDC within
60 seconds after the impact as specified in ANNEX 1.3.5. and ANNEX 1.3.5.2.2.
5.3.2.2.2. Isolation resistance
The criteria specified in the paragraphs 5.3.2.2.2.1. and 5.3.2.2.2.2. below shall be met.
The measurement shall be conducted in accordance with paragraph ANNEX 1.3.5.2.3. of paragraph
ANNEX 1.3.5.
5.3.2.2.2.1. Electrical power train consisting of separate DC- and AC-buses
If the AC high voltage buses and the DC high voltage buses are conductively isolated from each other,
isolation resistance between the high voltage bus and the electrical chassis (Ri, as defined in paragraph
ANNEX 1.3.5.2.3.) shall have a minimum value of 100 Ω/volt of the working voltage for DC buses, and
a minimum value of 500 Ω/volt of the working voltage for AC buses.
5.3.2.2.2.2. Electrical power train consisting of combined DC- and AC-buses
If the AC high voltage buses and the DC high voltage buses are conductively connected they shall meet
one of the following requirements:
(a)
Isolation resistance between the high voltage bus and the electrical chassis (Ri, as defined in paragraph
ANNEX 1.3.5.2.3.) shall have a minimum value of 500 Ω/volt of the working voltage;
(b)
Isolation resistance between the high voltage bus and the electrical chassis (Ri, as defined in paragraph
ANNEX 1.3.5.2.3.) shall have a minimum value of 100 Ω/volt of the working voltage and the AC bus
meets the physical protection as described in 5.3.2.2.3. ;
(c)
Isolation resistance between the high voltage bus and the electrical chassis (Ri, as defined in paragraph
ANNEX 1.3.5.2.3.) shall have a minimum value of 100 Ω/volt of the working voltage and the AC bus
meets the absence of high voltage as described in 5.3.2.2.1.
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5.3.2.2.3. Physical protection
Individual Contracting Parties may elect to adopt the physical protection. For protection against direct
contact with high voltage live parts, the protection degree IPXXB shall be provided.
In addition, for protection against electric shock which could arise from indirect contact, the resistance
between all exposed conductive parts and electrical chassis shall be lower than 0.1 ohm when there is
current flow of at least 0.2 amperes.
This requirement is satisfied if the galvanic connection has been established by welding. In case of
doubts a measurement shall be made.
5.3.2.3. Electrolyte spillage
In the period from the impact until 30 minutes after no electrolyte from the REESS shall spill into the
passenger compartment and no more than 7 per cent of electrolyte shall spill from the REESS outside
the passenger compartment.
The manufacturer shall demonstrate compliance in accordance with paragraph ANNEX 1.3.5.2.
ANNEX 1.
5.3.2.4. REESS retention
REESS located inside the passenger compartment shall remain in the location in which they are
installed and REESS components shall remain inside REESS boundaries.
No part of any REESS that is located outside the passenger compartment for electric safety assessment
shall enter the passenger compartment during or after the impact test.
The manufacturer shall demonstrate compliance in accordance with paragraph ANNEX 1.3.5.2.7.
ANEX 1 Test conditions and procedures
1.
Compliance tests for fuel system integrity
1.1.
Post-crash compressed hydrogen storage system leak test
The crash tests used to evaluate post-crash hydrogen leakage are those already applied in the jurisdictions of
each contracting party.
Prior to conducting the crash test, instrumentation is installed in the hydrogen storage system to perform the
required pressure and temperature measurements if the standard vehicle does not already have
instrumentation with the required accuracy.
The storage system is then purged, if necessary, following manufacturer directions to remove impurities from
the container before filling the storage system with compressed hydrogen or helium gas. Since the
storage system pressure varies with temperature, the targeted fill pressure is a function of the
temperature. The target pressure shall be determined from the following equation:
Ptarget = NWP x (273 + To) / 288
where NWP is the nominal working pressure (MPa), To is the ambient temperature to which the storage system
is expected to settle, and Ptarget is the targeted fill pressure after the temperature settles.
The container is filled to a minimum of 95 per cent of the targeted fill pressure and allowed to settle (stabilize)
prior to conducting the crash test.
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The main stop valve and shut-off valves for hydrogen gas, located in the downstream hydrogen gas piping, are
kept open immediately prior to the impact.
1.1.1. Post-crash leak test - compressed hydrogen storage system filled with compressed hydrogen
The hydrogen gas pressure, P0 (MPa), and temperature, T0 (°C), is measured immediately before the impact
and then at a time interval, Δt (min), after the impact. The time interval, Δt, starts when the vehicle
comes to rest after the impact and continues for at least 60 minutes. The time interval, Δt, is increased
if necessary in order to accommodate measurement accuracy for a storage system with a large volume
operating up to 70MPa; in that case, Δt can be calculated from the following equation:
Δt = VCHSS x NWP /1000 x ((-0.027 x NWP +4) x Rs – 0.21) -1.7 x Rs
where Rs = Ps / NWP, Ps is the pressure range of the pressure sensor (MPa), NWP is the Nominal Working
Pressure (MPa), VCHSS is the volume of the compressed hydrogen storage system (L), and Δt is the time
interval (min). If the calculated value of Δt is less than 60 minutes, Δt is set to 60 minutes.
The initial mass of hydrogen in the storage system can be calculated as follows:
Po’ = Po x 288 / (273 + T0)
ρo’ = –0.0027 x (P0’(2 + 0.75 x P0’ + 0.5789
Mo = ρo’ x VCHSS
Correspondingly, the final mass of hydrogen in the storage system, Mf, at the end of the time interval, Δt, can
be calculated as follows:
Pf’ = Pf x 288 / (273 + Tf)
ρf’ = –0.0027 x (Pf’(2 + 0.75 x Pf’ + 0.5789
Mf = ρf’ x VCHSS
where Pf is the measured final pressure (MPa) at the end of the time interval, and Tf is the measured final
temperature )°C(.
The average hydrogen flow rate over the time interval (that shall be less than the criteria in 5.2.2.1.) is
therefore
VH2 = (Mf-Mo) / Δt x 22.41 / 2.016 x (Ptarget /Po)
where VH2 is the average volumetric flow rate (NL/min) over the time interval and the term (Ptarget /Po) is used
to compensate for differences between the measured initial pressure, Po, and the targeted fill pressure
Ptarget.
1.1.2. Post-crash leak test - Compressed hydrogen storage system filled with compressed helium
The helium gas pressure, P0 (MPa), and temperature T0 )°C(, are measured immediately before the impact and
then at a predetermined time interval after the impact. The time interval, Δt, starts when the vehicle
comes to rest after the impact and continues for at least 60 minutes.
The time interval, Δt, shall be increased if necessary in order to accommodate measurement accuracy for a
storage system with a large volume operating up to 70MPa; in that case, Δt can be calculated from the
following equation:
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Δt = VCHSS x NWP /1000 x ((-0.028 x NWP +5.5) x Rs – 0.3) – 2.6 x Rs
where Rs = Ps / NWP, Ps is the pressure range of the pressure sensor (MPa), NWP is the Nominal Working
Pressure (MPa), VCHSS is the volume of the compressed storage system (L), and Δt is the time interval
(min). If the value of Δt is less than 60 minutes, Δt is set to 60 minutes.
The initial mass of hydrogen in the storage system is calculated as follows:
Po’ = Po x 288 / (273 + T0)
ρo’ = –0.0043 x (P0’(2 + 1.53 x P0’ + 1.49
Mo = ρo’ x VCHSS
The final mass of hydrogen in the storage system at the end of the time interval, Δt, is calculated as follows:
Pf’ = Pf x 288 / (273 + Tf)
ρf’ = –0.0043 x (Pf’(2 + 1.53 x Pf’ + 1.49
Mf = ρf’ x VCHSS
where Pf is the measured final pressure (MPa) at the end of the time interval, and Tf is the measured final
temperature (°C).
The average helium flow rate over the time interval is therefore
VHe = (Mf-Mo) / Δt x 22.41 / 4.003 x (Po/ Ptarget)
where VHe is the average volumetric flow rate (NL/min) over the time interval and the term Po/ Ptarget is used to
compensate for differences between the measured initial pressure (Po) and the targeted fill pressure
(Ptarget).
Conversion of the average volumetric flow of helium to the average hydrogen flow is done with the following
expression:
VH2 = VHe / 0.75
where VH2 is the corresponding average volumetric flow of hydrogen (that shall be less than the criteria in
5.2.2.1. to pass).
1.2.
Post-crash concentration test for enclosed spaces
The measurements are recorded in the crash test that evaluates potential hydrogen (or helium) leakage ( 1.1.
test procedure).
Sensors are selected to measure either the build-up of the hydrogen or helium gas or the reduction in oxygen
(due to displacement of air by leaking hydrogen/helium).
Sensors are calibrated to traceable references to ensure an accuracy of ±5 per cent at the targeted criteria of 4
per cent hydrogen or 3 per cent helium by volume in air, and a full scale measurement capability of at
least 25 per cent above the target criteria. The sensor shall be capable of a 90 per cent response to a full
scale change in concentration within 10 seconds.
Prior to the crash impact, the sensors are located in the passenger, luggage, and cargo compartments of the
vehicle as follows:
(a)
At a distance within 250 mm of the headliner above the driver’s seat or near the top centre the
passenger compartment;
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(b)
At a distance within 250 mm of the floor in front of the rear (or rear most) seat in the passenger
compartment;
(c)
At a distance within 100 mm of the top of luggage and cargo compartments within the vehicle that are
not directly affected by the particular crash impact to be conducted.
The sensors are securely mounted on the vehicle structure or seats and protected for the planned crash test
from debris, air bag exhaust gas and projectiles. The measurements following the crash are recorded
by instruments located within the vehicle or by remote transmission.
The vehicle may be located either outdoors in an area protected from the wind and possible solar effects or
indoors in a space that is large enough or ventilated to prevent the build-up of hydrogen to more than
10 per cent of the targeted criteria in the passenger, luggage, and cargo compartments.
Post-crash data collection in enclosed spaces commences when the vehicle comes to a rest. Data from the
sensors are collected at least every 5 seconds and continue for a period of 60 minutes after the test. A
first-order lag (time constant) up to a maximum of 5 seconds may be applied to the measurements to
provide "smoothing" and filter the effects of spurious data points.
The filtered readings from each sensor shall be below the targeted criteria of 3±1.0 per cent for hydrogen and
2.25 ± 0.75 per cent for helium at all times throughout the 60 minutes post-crash test period.
1.3.
Compliance test for single failure conditions
Either test procedure of 1.3.1. or 1.3.2. shall be executed:
1.3.1. Test procedure for vehicle equipped with hydrogen gas leakage detectors
1.3.1.1.Test condition
1.3.1.1.1 Test vehicle: The propulsion system of the test vehicle is started, warmed up to its normal operating
temperature, and left operating for the test duration. If the vehicle is not a fuel cell vehicle, it is warmed
up and kept idling. If the test vehicle has a system to stop idling automatically, measures are taken so
as to prevent the engine from stopping.
1.3.1.1.2. Test gas: Two mixtures of air and hydrogen gas: 2 ± 1.0 per cent concentration (or less) of hydrogen
in the air to verify function of the warning, and 3±1.0 per cent concentration (or less) of hydrogen in
the air to verify function of the shut-down. The proper concentrations are selected based on the
recommendation (or the detector specification) by the manufacturer.
1.3.1.2. Test method
1.3.1.2.1. Preparation for the test: The test is conducted without any influence of wind.
(a)
A test gas induction hose is attached to the hydrogen gas leakage detector;
(b)
The hydrogen leak detector is enclosed with a cover to make gas stay around hydrogen leak detector.
1.3.1.2.2. Execution of the test
(a)
Test gas is blown to the hydrogen gas leakage detector;
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(b)
Proper function of the warning system is confirmed when tested with the gas to verify function of the
warning;
(c)
The main shut-off valve is confirmed to be closed when tested with the gas to verify function of the
shut-down. For example, the monitoring of the electric power to the shut-off valve or of the sound of
the shut-off valve activation may be used to confirm the operation of the main shut-off valve of the
hydrogen supply.
1.3.2. Test procedure for integrity of enclosed spaces and detection systems.
1.3.2.1. Preparation:
1.3.2.1.1. The test is conducted without any influence of wind.
1.3.2.1.2. Special attention is paid to the test environment as during the test flammable mixtures of hydrogen
and air may occur.
1.3.2.1.3. Prior to the test the vehicle is prepared to allow remotely controllable hydrogen releases from the
hydrogen system. The number, location and flow capacity of the release points downstream of the
main hydrogen shutoff valve are defined by the vehicle manufacturer taking worst case leakage
scenarios into account. As a minimum, the total flow of all remotely controlled releases shall be
adequate to trigger demonstration of the automatic "warning" and hydrogen shut-off functions.
1.3.2.1.4. For the purpose of the test, a hydrogen concentration detector is installed where hydrogen gas may
accumulate most in the passenger compartment (e.g. near the headliner) when testing for compliance
with 5.2.1.4.2. and hydrogen concentration detectors are installed in enclosed or semi enclosed
volumes on the vehicle where hydrogen can accumulate from the simulated hydrogen releases when
testing
for
compliance
with
5.2.1.4.3.
(see
1.3.2.1.3.).
1.3.2.2. Procedure:
1.3.2.2.1. Vehicle doors, windows and other covers are closed.
1.3.2.2.2. The propulsion system is started , allowed to warm up to its normal operating temperature and left
operating at idle for the test duration.
1.3.2.2.3. A leak is simulated using the remote controllable function.
1.3.2.2.4. The hydrogen concentration is measured continuously until the concentration does not rise for 3
minutes. When testing for compliance with 5.2.1.4.3., the simulated leak is then increased using the
remote controllable function until the main hydrogen shutoff valve is closed and the tell-tale warning
signal is activated. The monitoring of the electric power to the shut-off valve or of the sound of the
shut-off valve activation may be used to confirm the operation of the main shut-off valve of the
hydrogen supply.
1.3.2.2.5. When testing for compliance with 5.2.1.4.2., the test is successfully completed if the hydrogen
concentration in the passenger compartment does not exceed 1.0 per cent. When testing for
compliance with 5.2.1.4.3., the test is successfully completed if the tell-tale warning and shut-off
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function are executed at (or below) the levels specified in 5.2.1.4.3.; otherwise, the test is failed and
the system is not qualified for vehicle service.
1.4.
Compliance test for the vehicle exhaust system
1.4.1. The power system of the test vehicle (e.g. fuel cell stack or engine) is warmed up to its normal operating
temperature.
1.4.2. The measuring device is warmed up before use to its normal operating temperature.
1.4.3. The measuring section of the measuring device is placed on the centre line of the exhaust gas flow
within 100 mm from the exhaust gas outlet external to the vehicle.
1.4.4. The exhaust hydrogen concentration is continuously measured during the following steps:
(a)
The power system is shut down;
(b)
Upon completion of the shut-down process, the power system is immediately started;
(c)
After a lapse of one minute, the power system is turned off and measurement continues until the power
system shut-down procedure is completed.
1.4.5. The measurement device shall have a measurement response time of less than 300 milliseconds.
1.5.
Compliance test for fuel line leakage
1.5.1. The power system of the test vehicle (e.g. fuel cell stack or engine) is warmed up and operating at its
normal operating temperature with the operating pressure applied to fuel lines.
1.5.2. Hydrogen leakage is evaluated at accessible sections of the fuel lines from the high-pressure section to
the fuel cell stack (or the engine), using a gas detector or leak detecting liquid, such as soap solution.
1.5.3. Hydrogen leak detection is performed primarily at joints
1.5.4. When a gas leak detector is used, detection is performed by operating the leak detector for at least 10
seconds at locations as close to fuel lines as possible.
1.5.5. When a leak detecting liquid is used, hydrogen gas leak detection is performed immediately after
applying the liquid. In addition, visual checks are performed a few minutes after the application of
liquid in order to check for bubbles caused by trace leaks.
1.
Installation verification
The system is visually inspected for compliance.
2.
Test procedures for compressed hydrogen storage
2.1.
Test procedures for qualification requirements of compressed hydrogen storage are organized as
follows:
Section 2.2 is the test procedures for baseline performance metrics (requirement of 5.1.1.)
Paragraph 2.3 is the test procedures for performance durability (requirement of 5.1.2.)
Paragraph 2.4 is the test procedures for expected on-road performance (requirement of 5.1.3.)
Paragraph 2.5 is the test procedures for service terminating performance in Fire (requirement of
5.1.4.)
Paragraph 2.6 is the test procedures for performance durability of primary closures (requirement of
5.1.5.)
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2.2.
Test procedures for baseline performance metrics (requirement of 5.1.1.)
2.2.1. Burst test (hydraulic)
The burst test is conducted at 20(±5(°C using a non-corrosive fluid. The rate of pressurization is less than or
equal to 1.4 MPa/s for pressures higher than 150 per cent of the nominal working pressure. If the rate
exceeds 0.35 MPa/s at pressures higher than 150 per cent NWP, then either the container is placed in
series between the pressure source and the pressure measurement device, or the time at the pressure
above a target burst pressure exceeds 5 seconds. The burst pressure of the container shall be recorded.
2.2.2. Pressure cycling test (hydraulic)
The test is performed in accordance with the following procedure:
(a)
The container is filled with a non-corrosive fluid;
(b)
The container and fluid are stabilized at the specified temperature and relative humidity at the start of
testing; the environment, fuelling fluid and container skin are maintained at the specified temperature
for the duration of the testing. The container temperature may vary from the environmental
temperature during testing;
(c)
The container is pressure cycled between 2 (±1) MPa and the target pressure at a rate not exceeding
10 cycles per minute for the specified number of cycles;
(d)
The temperature of the hydraulic fluid within the container is maintained and monitored at the
specified temperature.
2.3.
Test procedures for performance durability (requirement of 5.1.2.)
2.3.1. Proof pressure test
The system is pressurized smoothly and continually with a non-corrosive hydraulic fluid until the target test
pressure level is reached and then held for the specified time.
2.3.2. Drop (impact) test (unpressurized)
The storage container is drop tested at ambient temperature without internal pressurization or attached valves.
The surface onto which the containers are dropped shall be a smooth, horizontal concrete pad or other
flooring type with equivalent hardness.
(a)
The orientation of the container being dropped (per requirement of 5.1.2.2.) is determined as follows:
One or more additional container(s) shall be dropped in each of the orientations described below. The
drop orientations may be executed with a single container or as many as four containers may be used
to accomplish the four drop orientations.
(i)
Dropped once from a horizontal position with the bottom 1.8 m above the surface onto which it is
dropped;
(ii)
Dropped once onto the end of the container from a vertical position with the ported end upward with
a potential energy of not less than 488 J, with the height of the lower end no greater than 1.8 m;
(iii) Dropped once onto the end of the container from a vertical position with the ported end downward
with a potential energy of not less than 488 J, with the height of the lower end no greater than 1.8 m. If
the container is symmetrical (identical ported ends), this drop orientation is not required;
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(iv)
Dropped once at a 45° angle from the vertical orientation with a ported end downward with its centre
of gravity 1.8 m above the ground. However, if the bottom is closer to the ground than 0.6 m, the drop
angle shall be changed to maintain a minimum height of 0.6 m and a centre of gravity of 1.8 m above
the ground.
The four drop orientations are illustrated below.
Figure 5
Drop orientations
No attempt shall be made to prevent the bouncing of containers, but the containers may be prevented from
falling over during the vertical drop test described in b) above.
If more than one container is used to execute all three drop specifications, then those containers shall undergo
pressure cycling according to 2.2.2. until either leakage or 22,000 cycles without leakage have
occurred. Leakage shall not occur within number of Cycles (5,500, 7,500 or 11,000).
The orientation of the container being dropped per requirement 5.1.2.2. shall be identified as follows:
(a)
If a single container was subjected to all four drop orientations, then the container being dropped per
requirement of 5.1.2.2. shall be dropped in all four orientations;
(b)
If more than one container is used to execute the four drop orientations, and if all containers reach
22,000 cycles without leakage, then the orientation of the container being dropped per requirement
5.1.2.2. is the 45o orientation (iv), and that container shall then undergo further testing as specified in
paragraph 5.1.2.;
(c)
If more than one container is used to execute the four drop orientations and if any container does not
reach 22,000 cycles without leakage, then the new container shall be subjected to the drop
orientation(s) that resulted in the lowest number of cycles to leakage and then will undergo further
testing as specified in paragraph 5.1.2.
1.8m
> 488J
< 1.8 m
45o
> 0.6m
No. 1
N o.2
No.
3*
No.
4
center of gravity
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2.3.3. Surface damage test (unpressurized)
The test proceeds in the following sequence:
(a)
Surface flaw generation: Two longitudinal saw cuts are made on the bottom outer surface of the
unpressurized horizontal storage container along the cylindrical zone close to but not in the shoulder
area. The first cut is at least 1.25 mm deep and 25 mm long toward the valve end of the container. The
second cut is at least 0.75 mm deep and 200 mm long toward the end of the container opposite the
valve;
(b)
Pendulum impacts: The upper section of the horizontal storage container is divided into five distinct
(not overlapping) areas 100 mm in diameter each (see Figure 6). After 12 hours preconditioning at –
40 °C in an environmental chamber, the centre of each of the five areas sustains the impact of a
pendulum having a pyramid with equilateral faces and square base, the summit and edges being
rounded to a radius of 3 mm. The centre of impact of the pendulum coincides with the centre of gravity
of the pyramid. The energy of the pendulum at the moment of impact with each of the five marked
areas on the container is 30 J. The container is secured in place during pendulum impacts and not under
pressure.
Figure 6
Side view of tank
2.3.4. Chemical exposure and ambient temperature pressure cycling test
Each of the 5 areas of the unpressurized container preconditioned by pendulum impact (paragraph 4.2.5.2.) is
exposed to one of five solutions:
(a)
19 per cent (by volume) sulphuric acid in water (battery acid);
(b)
25 per cent (by weight) sodium hydroxide in water;
(c)
5 per cent (by volume) methanol in gasoline (fluids in fuelling stations);
(d)
28 per cent (by weight) ammonium nitrate in water (urea solution); and
(e)
50 per cent (by volume) methyl alcohol in water (windshield washer fluid).
The test container is oriented with the fluid exposure areas on top. A pad of glass wool approximately
0.5 mm thick and 100 mm in diameter is placed on each of the five preconditioned areas. A sufficient
amount of the test fluid is applied to the glass wool sufficient to ensure that the pad is wetted across its
surface and through its thickness for the duration of the test.
“Side” View of Tank
“Side” View of Tank
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The exposure of the container with the glass wool is maintained for 48 hrs with the container held at
125 per cent NWP )applied hydraulically( and 20 )±5( °C before the container is subjected to further
testing.
Pressure cycling is performed to the specified target pressures according to paragraph 2.2.2. at 20 (±5)
°C for the specified numbers of cycles. The glass wool pads are removed and the container surface is
rinsed with water the final 10 cycles to specified final target pressure are conducted.
2.3.5. Static pressure test (hydraulic)
The storage system is pressurized to the target pressure in a temperature-controlled chamber. The temperature
of the chamber and the non-corrosive fuelling fluid is held at the target temperature within ±5°C for
the specified duration.
2.4.
Test procedures for expected on-road performance (5.1.3.)
(Pneumatic test procedures are provided; hydraulic test elements are described in 3.2.)
2.4.1. Gas pressure cycling test (pneumatic)
At the onset of testing, the storage system is stabilized at the specified temperature, relative humidity and fuel
level for at least 24 hrs. The specified temperature and relative humidity is maintained within the test
environment throughout the remainder of the test. (When required in the test specification, the system
temperature is stabilized at the external environmental temperature between pressure cycles.) The
storage system is pressure cycled between less than 2(+0/-1) MPa and the specified maximum
pressure (±1MPa). If system controls that are active in vehicle service prevent the pressure from
dropping below a specified pressure, the test cycles shall not go below that specified pressure. The fill
rate is controlled to a constant 3-minute pressure ramp rate, but with the fuel flow not to exceed 60
g/s; the temperature of the hydrogen fuel dispensed to the container is controlled to the specified
temperature. However, the pressure ramp rate should be decreased if the gas temperature in the
container exceeds +85°C. The defuelling rate is controlled to greater than or equal to the intended
vehicle’s maximum fuel-demand rate. The specified number of pressure cycles is conducted. If devices
and/or controls are used in the intended vehicle application to prevent an extreme internal
temperature, the test may be conducted with these devices and/or controls (or equivalent measures).
2.4.2. Gas permeation test (pneumatic)
A storage system is fully filled with hydrogen gas at 115 per cent NWP (full fill density equivalent to 100 per
cent NWP at +15 °C is 113 per cent NWP at +55 °C( and held at +55 °C in a sealed container until
steady-state permeation or 30 hours, whichever is longer. The total steady-state discharge rate due to
leakage and permeation from the storage system is measured.
2.4.3. Localized gas leak test (pneumatic)
A bubble test may be used to fulfil this requirement. The following procedure is used when conducting the
bubble test:
(a)
The exhaust of the shutoff valve (and other internal connections to hydrogen systems) shall be capped
for this test (as the test is focused at external leakage).
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At the discretion of the tester, the test article may be immersed in the leak-test fluid or leak-test fluid
applied to the test article when resting in open air. Bubbles can vary greatly in size, depending on
conditions. The tester estimates the gas leakage based on the size and rate of bubble formation.
(b)
Note: For a localized rate of 0.005 mg/sec (3.6 NmL/min), the resultant allowable rate of bubble
generation is about 2,030 bubbles per minute for a typical bubble size of 1.5 mm in diameter. Even if
much larger bubbles are formed, the leak should be readily detectable. For an unusually large bubble
size of 6 mm in diameter, the allowable bubble rate would be approximately 32 bubbles per minute.
2.5.
Test procedures for service terminating performance in fire ( 5.1.4.)
2.5.1. Fire test
The hydrogen container assembly consists of the compressed hydrogen storage system with additional
relevant features, including the venting system (such as the vent line and vent line covering) and any
shielding affixed directly to the container (such as thermal wraps of the container(s) and/or
coverings/barriers over the TPRD(s)).
Either one of the following two methods are used to identify the position of the system over the initial
(localized) fire source:
2.5.1.1. Method 1: Qualification for a generic (non-Specific) vehicle installation
If a vehicle installation configuration is not specified (and the qualification of the system is not limited
to a specific vehicle installation configuration) then the localized fire exposure area is the area on the
test article farthest from the TPRD(s). The test article, as specified above, only includes thermal
shielding or other mitigation devices affixed directly to the container that are used in all vehicle
applications. Venting system(s) (such as the vent line and vent line covering) and/or coverings/barriers
over the TPRD(s) are included in the container assembly if they are anticipated for use in any
application. If a system is tested without representative components, retesting of that system is
required if a vehicle application specifies the use of these type of components.
2.5.1.2. Method 2: Qualification for a specific vehicle installation
If a specific vehicle installation configuration is specified and the qualification of the system is limited
to that specific vehicle installation configuration, then the test setup may also include other vehicle
components in addition to the hydrogen storage system. These vehicle components (such as shielding
or barriers, which are permanently attached to the vehicle’s structure by means of welding or bolts and
not affixed to the storage system) shall be included in the test setup in the vehicle-installed
configuration relative to the hydrogen storage system. This localized fire test is conducted on the worst
case localized fire exposure areas based on the four fire orientations: fires originating from the direction
of the passenger compartment, cargo/luggage compartment, wheel wells or ground-pooled gasoline.
The container may be subjected to engulfing fire without any shielding components, as described in
paragraph 2.5.2.
The following test requirements apply whether Method 1 or 2 (above) is used:
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(a)
The container assembly is filled with compressed hydrogen gas at 100 per cent of NWP. The container
assembly is positioned horizontally approximately 100 mm above the fire source. (Note: as stated
in 5.1.4., contracting parties under the 1998 Agreement may choose to use compressed air as an
alternative test gas for certification of the container for use in their countries or regions.) ;
Localized portion of the fire test
(b)
The localized fire exposure area is located on the test article furthest from the TPRD(s). If Method 2 is
selected and more vulnerable areas are identified for a specific vehicle installation configuration, the
more vulnerable area that is furthest from the TPRD(s) is positioned directly over the initial fire source;
(c)
The fire source consists of LPG burners configured to produce a uniform minimum temperature on the
test article measured with a minimum 5 thermocouples covering the length of the test article up to 1.65
m maximum (at least 2 thermocouples within the localized fire area, and at least 3 thermocouples
equally spaced and no more than 0.5 m apart in the remaining area) located 25 mm ± 10mm from the
outside surface of the test article along its longitudinal axis. At the option of the manufacturer or testing
facility, additional thermocouples may be located at TPRD sensing points or any other locations for
optional diagnostic purposes;
(d)
Wind shields are applied to ensure uniform heating;
(e)
The fire source initiates within a 250 mm ±50 mm longitudinal expanse positioned under the localized
exposure area of the test article. The width of the fire source encompasses the entire diameter (width)
of the storage system. If Method 2 is selected, the length and width shall be reduced, if necessary, to
account for vehicle-specific features;
(f)
As shown in Figure 7 the temperature of the thermocouples in the localized fire area has increased
continuously to at least 300 °C within 1 minute of ignition, to at least 600 °C within 3 minutes of
ignition, and a temperature of at least 600 °C is maintained for the next 7 minutes. The temperature in
the localized fire area shall not exceed 900 °C during this period. Compliance to the thermal
requirements begins 1 minute after entering the period with minimum and maximum limits and is
based on a 1-minute rolling average of each thermocouple in the region of interest. (Note: The
temperature outside the region of the initial fire source is not specified during these initial 10 minutes
from the time of ignition.).
40
قرار مجلس الوزراء
لسنة2021
بشأن
النظام الإماراتي للمركبات الهيدروجينية
Figure 7
Temperature profile of fire test
Engulfing portion of the fire test
Within the next 2-minute interval, the temperature along the entire surface of the test article shall be
increased to at least 800 °C and the fire source is extended to produce a uniform temperature along the
entire length up to 1.65 meters and the entire width of the test article (engulfing fire). The minimum
temperature is held at 800°C, and the maximum temperature shall not exceed 1100 °C. Compliance to
thermal requirements begins 1 minute after entering the period with constant minimum and maximum
limits and is based on a 1-minute rolling average of each thermocouple.
The test article is held at temperature (engulfing fire condition) until the system vents through the
TPRD and the pressure falls to less than 1 MPa. The venting shall be continuous (without interruption),
and the storage system shall not rupture. An additional release through leakage (not including release
through the TPRD) that results in a flame with length greater than 0.5 m beyond the perimeter of the
applied flame shall not occur.
1
600o C
800o C
Localized Fire Exposure
Engulfing Fire
Minutes
12
10
300o C
3
Min
Temp
Localized Area
Engulfing Region Outside
Localized Area (burner
ramp rate)
Ignite
Main
Burner
0
41
قرار مجلس الوزراء
لسنة2021
بشأن
النظام الإماراتي للمركبات الهيدروجينية
Table 2
Summary of fire test protocol
Localized fire region
Time period
Engulfing fire region
(Outside the localized
fire region)
Action
Ignite Burners
0-1 minute
No Burner Operation
Minimum temperature
Not specified
Not specified
Maximum temperature Less than 900oC
Not specified
Action
Increase temperature
and stabilize fire
for start of
localized fire
exposure
1-3 minutes
No Burner Operation
Minimum temperature
Greater than 300oC
Not specified
Maximum temperature Less than 900oC
Not specified
Act
اقتباس هذه الوثيقة
قرار مجلس الوزراء بشأن النظام الإماراتي للمركبات الهيدروجينية، قرار مجلس الوزراء، رقم 42، بتاريخ 1 يناير 2021 — الجوهرة القانونية، أرشيف التشريعات الإماراتية.